JPS591591A - Adjustment of gas component in prechamber of dry coke quenching equipment - Google Patents

Adjustment of gas component in prechamber of dry coke quenching equipment

Info

Publication number
JPS591591A
JPS591591A JP11137782A JP11137782A JPS591591A JP S591591 A JPS591591 A JP S591591A JP 11137782 A JP11137782 A JP 11137782A JP 11137782 A JP11137782 A JP 11137782A JP S591591 A JPS591591 A JP S591591A
Authority
JP
Japan
Prior art keywords
gas
prechamber
component
chamber
adjusting
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.)
Granted
Application number
JP11137782A
Other languages
Japanese (ja)
Other versions
JPH0149188B2 (en
Inventor
Takayuki Utsu
宇津 隆之
Masami Fujiwara
藤原 正美
Kiyotaka Yamamoto
清隆 山本
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.)
IHI Corp
Original Assignee
IHI 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 IHI Corp filed Critical IHI Corp
Priority to JP11137782A priority Critical patent/JPS591591A/en
Publication of JPS591591A publication Critical patent/JPS591591A/en
Publication of JPH0149188B2 publication Critical patent/JPH0149188B2/ja
Granted legal-status Critical Current

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  • Coke Industry (AREA)

Abstract

PURPOSE:To prevent explosion, combustion, etc. of gas which tend to occur at the time of opening an oven cover, by introducing gas for component adjustment into a prechamber according to the amounts of combustible components in the gas within the prechamber. CONSTITUTION:An inlet pipe 15 for component adjusting gas (air and/or nitrogen) is connected to a prechamber 2 of a cooling tower 1 (3 is a cooling chamber) and a component analyzer 18 is connected to it via a gas sampling tube 17. The gas in the prechamber 2 is analyzed with the analyzer 18 and when the amount of combustible components (CO, H2) has reached the predetermined value, a flow rate controlling valve 14 is adjusted with controlling units 19 and 20 to introduce the adjusting gas through a pipe 15 so that the amount of combustible components in the gas within the prechamber 2 may be maintained below the predetermined value and the gas component within the prechamber 2 may be kept below the explosion limit.

Description

【発明の詳細な説明】 本発明は赤熱コークスの乾式消火設備(こおiするブリ
チャンバー内のガス成分調整方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for adjusting gas components in a dry extinguishing equipment for red-hot coke.

冷却塔上部に形成されるブリチャンバー内には、C01
H2等を多く含むコークス炉カス相当の成分をもつガス
が貯留されることになり、またこのガスは発熱量が高く
、さらに約1000″Cの高温度を有している。このた
め、コークス投入のために炉蓋を開けると、炉口周辺の
大気と接触して燃焼又は爆発を起こし、作業員の安全上
の問題を有すると共に、周辺機器に火災や爆発による悪
影響を及ぼしたり、或いは爆発による騒音、火炎による
目視上の問題を生じる等、種々の問題点を有していた。
Inside the buri chamber formed at the top of the cooling tower, C01
Gas with a component equivalent to coke oven dregs containing a large amount of H2 etc. will be stored, and this gas has a high calorific value and a high temperature of about 1000"C. If the furnace lid is opened for this reason, it may come in contact with the atmosphere around the furnace mouth and cause combustion or explosion, which poses a safety problem for the workers, and may also have an adverse effect on surrounding equipment due to fire or explosion. It had various problems, such as noise and visual problems caused by flames.

このため、ブリチャンバー内のガス成分を調整する方法
として、ブリチャンバーに設けた十部放敵管よりブリチ
ャンバー内のガスを大気に放散し、循環ガス(成分1I
11整されている)をブリチャンバー内に導くようにし
たものがある。
Therefore, as a method to adjust the gas components in the yellowtail chamber, the gas inside the yellowtail chamber is diffused into the atmosphere from a ten-piece discharge pipe installed in the yellowtail chamber, and the circulating gas (component 1I
11) is introduced into the yellowtail chamber.

しかし、この方法によると、高温・高カロリーのガスを
多量に大気に放散することになるので、熱経済上の問題
があると共に、含塵ガスをそのまま大気に放出するので
粉塵公害を引き起こし、またそのために前記放散カスを
燃焼させるための大型の燃焼装置を必要とする、等の問
題点を有していた。
However, with this method, a large amount of high-temperature, high-calorie gas is released into the atmosphere, which poses thermoeconomic problems, and dust-containing gas is released directly into the atmosphere, causing dust pollution. For this reason, there have been problems such as the need for a large-sized combustion device to burn the emitted scum.

本発明は、こうした従来方法のもつ問題点を解決すべく
なしたもので、プリチャンバー内に、空気又はN、ガス
或いはそれらの混合物からなる成分8111用ガスを導
入することにより、ブリチャンバ軸内ガスの成分調整を
行い、炉蓋開時におけるブリチャンバ軸内ガスの爆発燃
焼などを防止すると共に、ブリチャンバ軸内ガスのもつ
熱エネルギーの有効利用と放散による公害問題の発生防
止を図るようにしたコークス乾式消火設備におけるプリ
チャンバ゛−内ガス成分調整方法、に係るものである。
The present invention was made to solve the problems of the conventional method, and by introducing a gas for component 8111 consisting of air, N, gas, or a mixture thereof into the pre-chamber, the gas inside the pre-chamber shaft is reduced. The coke dry type is designed to prevent the explosion and combustion of the gas in the brie chamber shaft when the furnace lid is opened, as well as to effectively use the thermal energy of the gas in the brie chamber shaft and prevent pollution problems due to dissipation. This invention relates to a method for adjusting gas components in a prechamber in fire extinguishing equipment.

以下本発明の実施例を図面を参照しつつ説明する。Embodiments of the present invention will be described below with reference to the drawings.

第1図は本発明の方法を適用するコークス乾式消火設備
の一例を示すもので、図中1は」二部にプリチャンバー
2を有し下部に冷却室3を形成した冷却塔、4は除塵器
、5はボイラ、6はサイクロン、7は循環ファンを表わ
し、循環ガスを冷却塔1に導入して冷却室3内の赤熱コ
ークスを冷却し、該冷却によって昇温されたmiガスを
ボイラ5に導いて熱回収を行う循環ガス流路を構成して
いる。また図中8は上記循環ガス流路における冷却塔l
へのガス入側位置に設けて前記プリチャンバー2内圧力
を調整するようにした1部放散管、9は冷却塔1土部に
毅けられ、炉蓋10を外すことにより冷却塔1内部に赤
熱コークスを運搬して投入するコークスパケット11を
備えたコークス運搬設備、12は上部放散管、13は除
塵器4に設けた空気導入用希釈ファンを示す。
Figure 1 shows an example of coke dry extinguishing equipment to which the method of the present invention is applied. 5 is a boiler, 6 is a cyclone, and 7 is a circulation fan. Circulating gas is introduced into the cooling tower 1 to cool the red-hot coke in the cooling chamber 3, and the mi gas heated by the cooling is sent to the boiler 5. This constitutes a circulating gas flow path that conducts heat recovery. In addition, 8 in the figure indicates the cooling tower l in the circulating gas flow path.
A partial dispersion pipe 9 installed at the gas inlet side position to adjust the pressure inside the pre-chamber 2 is installed in the soil part of the cooling tower 1, and by removing the furnace cover 10, it can be inserted into the inside of the cooling tower 1. Coke conveying equipment includes a coke packet 11 for conveying and charging red-hot coke, 12 is an upper dispersion pipe, and 13 is a dilution fan for introducing air provided in the dust remover 4.

上記構成を有するコークス乾式消火設備の冷却塔1にお
いて、第2図に示す如く、プリチャンバ−2上部の炉蓋
10に、空気或いはN2ガス又は空気中N2ガス等の成
分調整ガスを流量調整弁14を介して導入する成分調整
ガス管15を接続する。またこの成分1iI11整ガス
管15は、プリチャンバー2の土部位置で赤熱コークス
16がif#槙しない位置に接続するようにしても良い
。また前記プリチャンバー2内のガスを採取管17を介
して取り出しその成分分析を行うようにした成分分析器
】8を設け、該成分分析器18により検出された可燃ガ
ス成分例えばC01H2の量がある値になると、それに
応じて前記流量1i11整弁14を開作動させるように
した制御装置19.20を設ける。
In the cooling tower 1 of the coke dry extinguishing equipment having the above configuration, as shown in FIG. A component adjustment gas pipe 15 introduced through the pipe is connected. Further, the component 1iI11 gas regulating pipe 15 may be connected to a position where the red-hot coke 16 does not mix if# in the soil part of the pre-chamber 2. Further, a component analyzer] 8 is provided to take out the gas in the pre-chamber 2 through a sampling pipe 17 and analyze its components, and the amount of combustible gas components such as C01H2 detected by the component analyzer 18 is determined. A control device 19.20 is provided which opens the flow rate 1i11 regulating valve 14 accordingly.

前記したプリチャンバー2内のガスは約1000°0の
高温であってC01H2が主成分である。従ってこのよ
うな高温雰囲気においては、CD、H2は0.があれば
直ちに燃焼することになる。
The gas in the pre-chamber 2 has a high temperature of about 1000°0 and contains C01H2 as its main component. Therefore, in such a high temperature atmosphere, CD and H2 are 0. If there is, it will burn immediately.

しかもプリチャンバー2」二部は、Co、H,の−軽い
成分が充満しているため、炉蓋開時、空気中のOfと反
応して燃焼し、特にC01H3の濃度が高いと急激な燃
焼のために爆発が生じる。
Furthermore, the second part of the pre-chamber 2 is filled with light components such as Co and H, so when the furnace lid is opened, it reacts with Of in the air and burns, and if the concentration of CO1H3 is particularly high, the combustion will be rapid. An explosion occurs because of this.

このため、成分分析器18によりプリチャンバー2内の
ガスの成分分析を行い、ガス中の可燃成分Go、H,の
量%がある設定値になると、その6Mに応じ制all装
置19.20により流量調整弁14を調整して成分調整
ガスを導入し、プリチャンバ゛−2内のガス中のCO,
H,の夫々又はその合計量がある設定値に維持されるか
、或いはある設定値以下の範囲に維持されるよう制御す
る。又は、プリチャンバー2内のガス中のC01H2の
夫々又はその合計量がある設定値を超えた時流量調整弁
14を開とする。このとき、成分調整ガスを空気と−し
た場合はC01H2を燃焼させて希釈し、またN2ガス
とした場合は単に希釈させるという作用によって成分1
tll整が行われる。
For this reason, the component analyzer 18 analyzes the components of the gas in the pre-chamber 2, and when the amount % of combustible components Go, H, in the gas reaches a certain set value, the control device 19.20 The flow rate adjustment valve 14 is adjusted to introduce the component adjustment gas, and the CO and CO in the gas in the prechamber 2 are
Control is performed so that each or the total amount of H, is maintained at a certain set value or within a range below a certain set value. Alternatively, when each or the total amount of C01H2 in the gas in the prechamber 2 exceeds a certain set value, the flow rate regulating valve 14 is opened. At this time, when the component adjustment gas is air, the CO1H2 is burned and diluted, and when N2 gas is used, the component is simply diluted.
Tll adjustment is performed.

また、プリチャンバー2内のガス成分中のC01H2が
増加するのは、赤熱コークスが持ち込む揮発分が原因な
ので、C01H3成分の増加はコークスの投入と因果関
係にある。このため、コークスの投入はコークス炉から
の釜出しにより事iJに知ることができるので、そのタ
イムスケジュールにより成分調整ガスの導入な手動弁操
作にて行うようにしたり、或いはコークス運搬設備9の
信号(シーケンス)によりオン・オフ操作することによ
り」二記手動操作を自動により行うことができる。
Furthermore, the increase in C01H2 in the gas components in the pre-chamber 2 is due to the volatile matter brought in by the red-hot coke, so the increase in the C01H3 component has a causal relationship with the addition of coke. For this reason, since the injection of coke can be known in advance by taking out the coke from the coke oven, depending on the time schedule, it can be carried out by manual valve operation such as introduction of composition adjustment gas, or by the signal of the coke transport equipment 9. By turning on and off according to the sequence (sequence), the manual operation described in (2) can be performed automatically.

更にまた、前記成分調整ガス管15をプリチャンバー2
士部に接続することにより、コークス投入と同時に成分
調整ガスを投入し、コークスの投入と同時に大略の成分
i11!整を行うようにすることもできる。
Furthermore, the component adjustment gas pipe 15 is connected to the pre-chamber 2.
By connecting to Shibe, component adjustment gas is added at the same time as coke is added, and the approximate composition i11 is added at the same time as coke is added. It is also possible to perform adjustments.

尚、本発明は上記実施例にのみ限定されるものではなく
、成分1111移り)ス管を空気用とN2ガス用に別々
に設けるようにしても良いこと、訓移ガス吠込オン・オ
フ操作用の弁と直列に流量調整弁を設け、1iIll整
ガス流量を調整しても良いこと、そのf小本発明の要旨
を逸脱しない範囲内において種々変更を加え得ること、
等は勿論である。
It should be noted that the present invention is not limited to the above-mentioned embodiments, and that the component 1111 gas pipes may be provided separately for air and N2 gas. A flow rate regulating valve may be provided in series with the valve for adjusting the gas flow rate, and various changes may be made within the scope of the present invention.
Of course, etc.

」=述した本発明のコークス乾式消火設備におけるブリ
チャンバ軸内カス成分調整方法によれは、吹のような優
れた効果を奏し得る。
The method for adjusting the waste component in the shaft of the brie chamber in the coke dry extinguishing equipment of the present invention described above can produce excellent effects such as blowing.

(1)ブリチャンバー内に、空気又はN2ガス或いはそ
れらの混合物からなる成分調整用ガスを導入することに
より、ブリチャンバ軸内ガスの成分調整を行うようにし
ているので、ブリチャンバ軸内ガスを上部放散管より大
気に放nkさせ、wI環ガスをブリチャンバーに導入す
ることなく成分調整することができる。
(1) The composition of the gas in the shaft of the Buri chamber is adjusted by introducing a gas for adjusting the composition consisting of air, N2 gas, or a mixture thereof into the Buri chamber. It is possible to adjust the composition of the wI ring gas without introducing it into the buri chamber by releasing it into the atmosphere from the tube.

(j)  ブリチャンバ軸内ガスを本装置を設けない場
合の様に多量に大気に放散させることがないので、放散
していたカスのもつエネルギーを有効に利用できる。
(j) Since a large amount of gas in the shaft of the brie chamber is not dissipated into the atmosphere as in the case where this device is not installed, the energy of the dissipated residue can be used effectively.

0の 含塵ガスの放散による公害問題を解法できる。The pollution problem caused by the dispersion of dust-containing gas can be solved.

Gの 簡単な装置にて容易に実施することができる。It can be easily carried out using a simple device.

(v)  ブリチャンバ軸内ガスの成分を分析し、その
ガス成分の可燃成分の量に基づいて成分調整用ガスをブ
リチャンバー内に導入することにより、プリチャンバ軸
内ガスの成分調整を確実に自動的に行わしめることがで
きる。
(v) By analyzing the components of the gas in the pre-chamber shaft and introducing a gas for composition adjustment into the pre-chamber based on the amount of combustible components in the gas component, the composition of the gas in the pre-chamber shaft can be reliably and automatically adjusted. It can be done.

(VD  ブリチャンバーに対する成分調整用ガスの導
入をコークス投入のタイムスケジュールに基づいて行う
ことにより実施の際の構成を更に簡略化することがごぎ
る。
(It is possible to further simplify the implementation configuration by introducing the component adjustment gas into the VD brie chamber based on the time schedule of coke injection.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明の方法を適用したコークス乾式消火設備
の一例を示す説明図、第2図は本発明の一実施例を示す
説明図である。 1は冷却塔、2はブリチャンバー、3は冷却室、4は除
塵器、5はボイラ、6はサイクロン、7は循環ファン、
9はコークス運搬設備、1oは炉蓋、14は流量調整弁
、15は成分調整ガス管、17は採取管、18は成分分
析器、19.20は制御装置を示す。 特許用1頭人 石川島播磨重工業株式会社 663
FIG. 1 is an explanatory diagram showing an example of coke dry extinguishing equipment to which the method of the present invention is applied, and FIG. 2 is an explanatory diagram showing an example of the present invention. 1 is a cooling tower, 2 is a buri chamber, 3 is a cooling room, 4 is a dust remover, 5 is a boiler, 6 is a cyclone, 7 is a circulation fan,
Reference numeral 9 indicates coke transport equipment, 1o a furnace lid, 14 a flow rate adjustment valve, 15 a component adjustment gas pipe, 17 a sampling pipe, 18 a component analyzer, and 19.20 a control device. 1 person for patent Ishikawajima Harima Heavy Industries Co., Ltd. 663

Claims (1)

【特許請求の範囲】 ■)ブリチャンバー内に成分調整用ガスを導入してブリ
チャンバー内のガスの成分を調整するに際し、ブリチャ
ンバ軸内ガスの成分を分析し、そのガス成分の可燃成分
の量に基づいて前記成分1I11整用ガスを導入するこ
とを特徴とするコークス乾式消火設備におけるブリチャ
ンバ軸内ガス成分調整方法。 2)ブリチャンバー内に成分調整用カスを導入してブリ
チャンバー内のガスの成分を調整するに際し、コークス
投入のタイムスケジュールに基づいて前記成分調整用ガ
スを導入することを特徴とするコークス乾式消火設備に
おけるプリチャンバ軸内ガス成分調整方法。
[Claims] ■) When adjusting the composition of the gas in the Buri chamber by introducing a component adjustment gas into the Buri chamber, the components of the gas in the shaft of the Buri chamber are analyzed, and the amount of combustible components in the gas component is analyzed. A method for adjusting gas components in a brie chamber shaft in coke dry extinguishing equipment, characterized by introducing the component 1I11 preparation gas based on the following. 2) Coke dry extinguishing characterized by introducing the component adjusting gas into the yellowtail chamber based on the time schedule of coke injection when adjusting the composition of the gas in the yellowtail chamber by introducing the component adjusting residue into the yellowtail chamber. A method for adjusting gas components in the prechamber shaft in equipment.
JP11137782A 1982-06-28 1982-06-28 Adjustment of gas component in prechamber of dry coke quenching equipment Granted JPS591591A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11137782A JPS591591A (en) 1982-06-28 1982-06-28 Adjustment of gas component in prechamber of dry coke quenching equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11137782A JPS591591A (en) 1982-06-28 1982-06-28 Adjustment of gas component in prechamber of dry coke quenching equipment

Publications (2)

Publication Number Publication Date
JPS591591A true JPS591591A (en) 1984-01-06
JPH0149188B2 JPH0149188B2 (en) 1989-10-23

Family

ID=14559639

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11137782A Granted JPS591591A (en) 1982-06-28 1982-06-28 Adjustment of gas component in prechamber of dry coke quenching equipment

Country Status (1)

Country Link
JP (1) JPS591591A (en)

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6137893A (en) * 1984-07-31 1986-02-22 Nippon Steel Chem Co Ltd Method and apparatus for dry quenching
JPS6172092A (en) * 1984-09-17 1986-04-14 Mitsubishi Heavy Ind Ltd Facility for dry-quenching of red heated coke
JPS61143488A (en) * 1984-12-18 1986-07-01 Mitsubishi Heavy Ind Ltd Coke dry extinugisher
JPS62585A (en) * 1985-06-26 1987-01-06 Sumikin Coke Co Ltd Method of preventing occurrence of detonation in opening feeding cover of dry quenching equipment for coke
JPS62215690A (en) * 1986-03-17 1987-09-22 Ishikawajima Harima Heavy Ind Co Ltd Cooling column of dry quenching installation for coke
JPS63101484A (en) * 1986-10-17 1988-05-06 Sumikin Chem Co Ltd Dry quenching method of coke
JPS6414295A (en) * 1987-07-08 1989-01-18 Nippon Steel Corp Method for preventing abnormal combustion at lid opening of cooling tower in coke dry quenching facilities
JPH02151687A (en) * 1988-12-05 1990-06-11 Nippon Steel Corp Method and device for raising temperature of lining refractory at start-up of coke dry quenching equipment
JPH0441586A (en) * 1990-06-07 1992-02-12 Nippon Steel Corp Increase and control of heat recovery in coke dry quenching facility
KR100503202B1 (en) * 2000-12-12 2005-07-25 주식회사 포스코 Apparatus for controlling the hot gas in the upper portion of the quenching tower

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS55110186A (en) * 1979-02-19 1980-08-25 Nippon Kokan Kk <Nkk> Dry quenching of coke

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS55110186A (en) * 1979-02-19 1980-08-25 Nippon Kokan Kk <Nkk> Dry quenching of coke

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6137893A (en) * 1984-07-31 1986-02-22 Nippon Steel Chem Co Ltd Method and apparatus for dry quenching
JPS6172092A (en) * 1984-09-17 1986-04-14 Mitsubishi Heavy Ind Ltd Facility for dry-quenching of red heated coke
JPS61143488A (en) * 1984-12-18 1986-07-01 Mitsubishi Heavy Ind Ltd Coke dry extinugisher
JPS62585A (en) * 1985-06-26 1987-01-06 Sumikin Coke Co Ltd Method of preventing occurrence of detonation in opening feeding cover of dry quenching equipment for coke
JPS62215690A (en) * 1986-03-17 1987-09-22 Ishikawajima Harima Heavy Ind Co Ltd Cooling column of dry quenching installation for coke
JPS63101484A (en) * 1986-10-17 1988-05-06 Sumikin Chem Co Ltd Dry quenching method of coke
JPS6414295A (en) * 1987-07-08 1989-01-18 Nippon Steel Corp Method for preventing abnormal combustion at lid opening of cooling tower in coke dry quenching facilities
JPH02151687A (en) * 1988-12-05 1990-06-11 Nippon Steel Corp Method and device for raising temperature of lining refractory at start-up of coke dry quenching equipment
JPH0441586A (en) * 1990-06-07 1992-02-12 Nippon Steel Corp Increase and control of heat recovery in coke dry quenching facility
KR100503202B1 (en) * 2000-12-12 2005-07-25 주식회사 포스코 Apparatus for controlling the hot gas in the upper portion of the quenching tower

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JPH0149188B2 (en) 1989-10-23

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