JPH10183131A - Change of pressure in furnace of coke furnace - Google Patents

Change of pressure in furnace of coke furnace

Info

Publication number
JPH10183131A
JPH10183131A JP34864196A JP34864196A JPH10183131A JP H10183131 A JPH10183131 A JP H10183131A JP 34864196 A JP34864196 A JP 34864196A JP 34864196 A JP34864196 A JP 34864196A JP H10183131 A JPH10183131 A JP H10183131A
Authority
JP
Japan
Prior art keywords
pressure
chamber
carbonization chamber
gas
combustion
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
JP34864196A
Other languages
Japanese (ja)
Inventor
Tsuneo Araki
常夫 荒木
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 Engineering Corp
Original Assignee
NKK Corp
Nippon Kokan Ltd
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 NKK Corp, Nippon Kokan Ltd filed Critical NKK Corp
Priority to JP34864196A priority Critical patent/JPH10183131A/en
Publication of JPH10183131A publication Critical patent/JPH10183131A/en
Pending legal-status Critical Current

Links

Landscapes

  • Coke Industry (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a method for changing a pressure in a furnace of a coke furnace for promoting a precipitation of SiO2 when repairing a furnace wall of the coke furnace by a gas containing SiCl4 . SOLUTION: A pressure in a combustion room is changed alternatively to negative and positive pressures after stopping the combustion in the combustion room 2 concerning with the repair of a furnace wall 3 by opening a waste valve 32 of the combustion room 2, forming the combustion room 2 into the negative pressure by communicating the combustion room to a flue 33, further closing the waste valve 32, blowing steam through a C gas-charging pipe 40 to the combustion room 2 to form the combustion room 2 into the positive pressure in the method for changing a pressure in a furnace of a coke furnace.

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、コークス炉の炉壁
の貫通損傷部に炭化室側からSiCl4 含有ガスを侵入さ
せ、または、炭化室側からSiCl4 含有ガスを侵入させる
とともに、燃焼室側から水蒸気を含んだ燃焼ガスを侵入
させることにより、貫通損傷部にSiO2を析出させて炉内
壁を補修する際、SiO2の析出を促進させるためのコーク
ス炉の炉内圧力変動方法に関するものである。
The present invention relates is the through damaged portion of the furnace wall of a coke oven to penetrate the SiCl 4 containing gas from the coking chamber side, or, together to penetrate the SiCl 4 containing gas from the carbonization chamber side, a combustion chamber by entering the combustion gas containing steam from the side, the through damaged portion when repairing the furnace inner wall by precipitating SiO 2, relates furnace pressure fluctuations method coke oven for promoting deposition of SiO 2 It is.

【0002】[0002]

【従来の技術】コークス炉では石炭を収納する炭化室と
加熱ガスを発生させる燃焼室とが炉壁を介して交互に配
置されている。加熱ガスによって炉壁が加熱され、炉壁
を通じて熱が炭化室の石炭に伝えられて、これが熱分解
して、石炭の乾留が進行する。ここで、炉壁は通常ケイ
石煉瓦が使用されている。厚さは50〜150mmであ
る。出来上がった高温のコークスはコークス炉両サイド
の押し出し側およびガイド車側の蓋を外し、押出機によ
りガイド車側へ排出される。次いで、次チャージの石炭
が上部の装炭口より装入され、上述と同様のサイクルが
繰り返される。炉壁は押し出されるコークスによる摩耗
や、加熱、冷却の繰り返しにより、目地切れ、煉瓦の破
損を起こす。これが炭化室と燃焼室が貫通する亀裂損傷
に至ると、乾留ガスが炭化室から燃焼室へ漏洩するので
石炭の乾留は、困難となる。このため、いくつかの補修
方法が適用されている。
2. Description of the Related Art In a coke oven, a carbonization chamber for accommodating coal and a combustion chamber for generating a heating gas are alternately arranged via a furnace wall. The furnace wall is heated by the heating gas, and heat is transferred to the coal in the coking chamber through the furnace wall, which is thermally decomposed and carbonization of the coal proceeds. Here, the furnace wall is usually made of silica brick. The thickness is 50-150 mm. The resulting high-temperature coke is removed from the extruder on both sides of the coke oven and the lid on the guide wheel side, and is discharged to the guide wheel side by an extruder. Next, the next charge coal is charged from the upper charging port, and the same cycle as described above is repeated. The furnace wall wears due to the extruded coke, and repeated heating and cooling causes breakage of joints and damage to bricks. If this leads to crack damage penetrating the carbonization chamber and the combustion chamber, carbonization of the coal becomes difficult because the carbonization gas leaks from the carbonization chamber to the combustion chamber. For this reason, several repair methods have been applied.

【0003】例えば、空にした炭化室へ耐火物粉末を空
気、窒素等の媒体を使用し、気流輸送にて貫通亀裂部の
閉塞を図る方法が知られている。および炉蓋近傍の炉壁
の補修方法として、耐火物粉末と水との混合物を損傷部
に吹き付ける湿式吹き付け法が知られているが、これら
は、一時的にガス漏れを減少させることは可能である
が、効果は長続きしない。
[0003] For example, a method is known in which a refractory powder is poured into an empty carbonization chamber by using a medium such as air or nitrogen and the through crack is closed by pneumatic transportation. As a method of repairing the furnace wall near the furnace lid, there is known a wet spraying method in which a mixture of refractory powder and water is sprayed on a damaged portion.However, these methods can temporarily reduce gas leakage. Yes, but the effect is not long lasting.

【0004】また、耐火物粉末を酸素−燃料ガスからな
る火炎中に供給するか、あるいはアルミニウムやケイ素
の燃焼で半溶融または溶融状態にして炉壁に接着させる
溶射法がある。この溶射法においては、溶融した溶射材
料は、被補修部に衝突し急冷凝固し、ガラス相を主体と
した溶射補修体を形成する。このガラス相は、冷却過程
でさらに結晶相に移転するが、その際に体積収縮が起こ
り、ひび割れが発生する。このため、溶射補修体は母材
との結合が不十分となり、長期にわたる使用に耐えな
い。特に、溶射に伴う局部加熱で母材が変質して強度低
下した場合には、母材側から亀裂が進展して溶射体が脱
落する。
[0004] Further, there is a thermal spraying method in which refractory powder is supplied into a flame composed of oxygen-fuel gas, or is adhered to a furnace wall in a semi-molten or molten state by burning aluminum or silicon. In this thermal spraying method, the molten thermal sprayed material collides with the repaired portion and rapidly solidifies to form a thermal spray repair body mainly composed of a glass phase. This glass phase is further transferred to a crystal phase during the cooling process, but at that time, volume shrinkage occurs and cracks occur. For this reason, the thermal spray repair body is insufficiently bonded to the base material, and cannot be used for a long time. In particular, when the base material is deteriorated due to local heating due to thermal spraying and the strength is reduced, cracks develop from the base material side and the sprayed material falls off.

【0005】また、炉壁を構成するケイ石煉瓦の損傷が
甚だしい場合には、損傷した煉瓦の積替えが行われる。
積替えは煉瓦の冷却に伴う損傷を避けるために熱間で行
われる。しかし、熱間での補修作業は高温重筋労働を伴
うだけでなく、長時間にわたってコークスの生産を停止
させるので経済的損失も大きい。
[0005] Further, when the silica bricks constituting the furnace wall are severely damaged, the damaged bricks are replaced.
Transshipments are done hot to avoid damage associated with brick cooling. However, hot repair work involves not only high-temperature heavy labor, but also a large economic loss because coke production is stopped for a long time.

【0006】このように、従来法には問題が多いが、従
来法の中では溶射法が優れ、施工した溶射体の耐用性に
も比較的優れているが、未だ不十分であり、溶射体の寿
命は、溶射体自身の強度や耐スポーリング性だけで決ま
らず、上述したような溶射体の脱落の問題もあり寿命は
約半年である。
As described above, the conventional method has many problems. Among the conventional methods, the thermal spraying method is excellent, and the durability of the applied thermal sprayed material is relatively excellent, but it is still insufficient. Is not determined only by the strength and spalling resistance of the sprayed body itself, and the service life is about half a year due to the problem of falling off of the sprayed body as described above.

【0007】コークス炉の炭化室と燃焼室との炉壁は、
炭化室から燃焼室に貫通する亀裂が無く、且つ平滑な壁
面を維持することが望ましい。従って、炉壁の強度およ
び耐摩耗性を向上させることが重要である。炉壁に貫通
亀裂が発生した場合には、炉壁の損傷部位の交換あるい
は溶射法による補修をしなければならない。上述したよ
うに、損傷部位の交換には装置の長時間にわたる運転停
止が必要となる。コークス炉のように、炉壁の保護のた
めに炉を冷却することが実質的に不可能な設備では、熱
間で炉壁を交換しなければならないという問題も発生す
る。
The furnace walls of the coke oven and the combustion chamber of the coke oven are:
It is desirable that there be no cracks penetrating from the carbonization chamber to the combustion chamber and that a smooth wall surface be maintained. Therefore, it is important to improve the strength and wear resistance of the furnace wall. If a through crack occurs in the furnace wall, the damaged wall must be replaced or repaired by thermal spraying. As mentioned above, replacing the damaged area requires a long shutdown of the device. In a facility such as a coke oven where it is practically impossible to cool the oven to protect the oven wall, there is also the problem that the oven wall must be exchanged hot.

【0008】本出願人は、上述した問題を解決するため
に、特願平07−303683号と特願平08−109
813号で方法1および2を提案した。これらの方法を
図5により次に説明する。1は炭化室、2は燃焼室、3
はSiO2を主成分としCaO2、Al 2O3 およびFe2O3 を合計で
5wt.%程度含み、開口率20%程度のケイ石煉瓦と
それを固定するSiO2を主成分とする目地からなるケイ石
煉瓦の炉壁、5は石炭の装入蓋である。コークス炉は炭
化室1と燃焼室2が炉壁3を間にして交互に連なってい
る。燃料と空気をガス入口4から燃焼室2に供給し、燃
焼ガス9を発生させ、この燃焼ガスの熱により炉壁3を
介して炭化室1を加熱した後、上部開口から図示しない
蓄熱室に排出する。6は炉壁3に発生した1mm以上の
開口部を有する貫通損傷部、7は1mm未満の微細な開
口部を有する貫通損傷部である。
[0008] The present applicant has solved the above-mentioned problem.
Japanese Patent Application Nos. 07-303683 and 08-109
No. 813 proposed methods 1 and 2. These methods
This will be described next with reference to FIG. 1 is a carbonization chamber, 2 is a combustion chamber, 3
Is SiOTwoWith CaO as the main componentTwo, Al TwoOThreeAnd FeTwoOThreeIn total
5 wt. %, With an opening ratio of about 20%
SiO fixing itTwoComposed of silica-based joints
The furnace wall 5 of the brick is a lid for charging coal. Coke oven charcoal
Chamber 1 and combustion chamber 2 are connected alternately with furnace wall 3 in between
You. Fuel and air are supplied from the gas inlet 4 to the combustion chamber 2,
The combustion gas 9 is generated, and the furnace wall 3 is heated by the heat of the combustion gas.
Not shown after heating the carbonization chamber 1 through the upper opening
Discharge to the heat storage room. 6 is 1 mm or more generated on the furnace wall 3
Penetration damaged part with opening, 7 is fine opening less than 1 mm
It is a penetration damage part having a mouth.

【0009】方法1は、上記の貫通損傷部の中で、微細
な開口部を有する貫通損傷部7の補修に適する方法であ
り、先ず、炭化室1を空窯の状態にして、装入蓋5に設
けたガス入口8からSiCl4 含有ガス10を炭化室1に供
給する。そして、炭化室1内圧力を燃焼室2内圧力より
高く保持し、貫通損傷部7の内部に浸透させる。次に、
炭化室1内圧力を燃焼室2内圧力より低く保持して、燃
焼ガス9を燃焼室2側から貫通損傷部7に浸透させる。
このように、炭化室1内圧力と燃焼室2内圧力の差を正
負に変動させることにより、貫通損傷部7にSiCl4 含有
ガス10と燃焼ガス9を交互に浸透させる。その結果、
SiCl4 ガスと燃焼ガス中のH2O (水蒸気)が反応してSi
O2が生成し、貫通損傷部7がこのSiO2により充填され
て、補修がなされる。
Method 1 is a method suitable for repairing a penetrating damaged portion 7 having a fine opening in the above-mentioned penetrating damaged portion. A SiCl 4 -containing gas 10 is supplied to the carbonization chamber 1 from a gas inlet 8 provided at 5. Then, the internal pressure of the carbonization chamber 1 is maintained higher than the internal pressure of the combustion chamber 2, and the internal pressure of the penetration chamber 7 is permeated. next,
The pressure inside the carbonization chamber 1 is kept lower than the pressure inside the combustion chamber 2, and the combustion gas 9 permeates into the penetration damage portion 7 from the combustion chamber 2 side.
As described above, the difference between the pressure in the carbonization chamber 1 and the pressure in the combustion chamber 2 is changed to positive or negative, so that the SiCl 4 -containing gas 10 and the combustion gas 9 permeate the penetration damage portion 7 alternately. as a result,
SiCl 4 gas reacts with H 2 O (steam) in the combustion gas to produce Si
O 2 is generated, and the penetrating damaged portion 7 is filled with the SiO 2 to perform repair.

【0010】方法2は、上記貫通損傷部の中で、比較的
大きな開口部を有する貫通損傷部6の補修に適する方法
であり、先ず炭化室1を空窯の状態にして、炭化室1側
から、MgO,CaO,ZrO2等の無機酸化物粉末を気流輸送し
て、貫通損傷部6に侵入させて無機酸化物粉末の充填体
を形成させる。次いで、装入蓋5に設けたガス入口8か
らSiCl4 含有ガス10を炭化室3に供給し、炭化室1内
圧力を燃焼室2内圧力より高く保持し、貫通損傷部6に
充填された無機酸化物粉末粒子間にSiCl4 含有ガス10
を浸透させる。無機酸化物粉末とSiCl4 含有ガス10と
を反応させてSiO2と塩化物を生成させる。次に、炭化室
1内圧力を燃焼室2内圧力より低く保持して、燃焼ガス
9を燃焼室2側から貫通損傷部6の充填体に浸透させ
る。燃焼ガス9中のH2O (水蒸気)が充填体中に副生し
た塩化物と反応して非SiO2の酸化物が生成する。このよ
うに、炭化室1内圧力と燃焼室2内圧力の差を正負に変
動させることにより、貫通損傷部6の充填体にSiCl4
有ガス10と燃焼ガス9を交互に浸透させる。その結
果、貫通損傷部6の充填体中にSiO2と非SiO2の酸化物が
生成し、充填体の密度が向上し、補修がなされる。
Method 2 is a method suitable for repairing a penetrating damaged portion 6 having a relatively large opening in the above penetrating damaged portion. Then, an inorganic oxide powder such as MgO, CaO, ZrO 2 or the like is transported by airflow, and penetrates into the penetrated damage portion 6 to form a packed body of the inorganic oxide powder. Next, a SiCl 4 -containing gas 10 was supplied to the coking chamber 3 from the gas inlet 8 provided in the charging lid 5, the pressure in the coking chamber 1 was kept higher than the pressure in the combustion chamber 2, and the penetrating damaged portion 6 was filled. SiCl 4 containing gas 10 between inorganic oxide powder particles
Infiltrate. The inorganic oxide powder is reacted with the SiCl 4 -containing gas 10 to generate SiO 2 and chloride. Next, the internal pressure of the carbonization chamber 1 is maintained lower than the internal pressure of the combustion chamber 2, and the combustion gas 9 permeates the filler of the penetration damaged portion 6 from the combustion chamber 2 side. H 2 O (steam) in the combustion gas 9 reacts with chloride by-produced in the packing to generate non-SiO 2 oxide. As described above, by changing the difference between the pressure in the carbonization chamber 1 and the pressure in the combustion chamber 2 to positive or negative, the SiCl 4 -containing gas 10 and the combustion gas 9 are alternately permeated into the filling material of the penetration damage portion 6. As a result, oxides of SiO 2 and non-SiO 2 are generated in the filling body of the penetrating damaged portion 6, the density of the filling body is improved, and repair is performed.

【0011】[0011]

【発明が解決しようとする課題】本発明は、コークス炉
の炉壁に発生した貫通損傷部にSiCl4 含有ガスと水蒸気
を交互に浸透させ、上記方法1または2による貫通損傷
部の補修を行うためのコークス炉の炉内圧力変動方法を
提供することを目的とする。
SUMMARY OF THE INVENTION According to the present invention, a penetrating damaged portion generated in a furnace wall of a coke oven is alternately infiltrated with a SiCl 4 -containing gas and water vapor, and the penetrating damaged portion is repaired by the above method 1 or 2. To provide a method of fluctuating the pressure in a coke oven for coke.

【0012】[0012]

【課題を解決するための手段】本発明は、上記目的を以
下の方法により達成する。
The present invention achieves the above object by the following method.

【0013】第1の方法は、炉壁の補修に係わる燃焼室
の燃焼を中止した後、該燃焼室のウエストバルブを開
き、前記燃焼室を煙道に連通させ燃焼室を負圧にし、次
に、前記ウエストバルブを閉じ、Cガス供給管を介して
前記燃焼室に水蒸気を吹込み、燃焼室を正圧にすること
により燃焼室の圧力を負圧と正圧に交互に変動させるコ
ークス炉の炉内圧力変動方法である。ここで、Cガスと
は、コークスガスのことである。
In the first method, after the combustion in the combustion chamber related to the repair of the furnace wall is stopped, the waist valve of the combustion chamber is opened, the combustion chamber is communicated with the flue, and the pressure in the combustion chamber is reduced. A coke oven that closes the waist valve, blows steam into the combustion chamber through a C gas supply pipe, and pressurizes the combustion chamber to alternately change the pressure of the combustion chamber to negative pressure and positive pressure. This is the method of fluctuating the pressure in the furnace. Here, C gas is coke gas.

【0014】第2の方法は、炉壁の補修に係る炭化室を
空にした後、密閉状態とし、送風機、配管系および配管
系を切り替える複数の弁からなるガス給排気装置を使用
して、最初に、前記複数の弁の開閉により配管系をガス
供給状態とし、ガスを前記炭化室に供給して炭化室を正
圧とし、次に、前記複数の弁の開閉を変え配管系をガス
排出状態とし、炭化室のガスを排出して炭化室を負圧に
することにより炭化室の圧力を負圧と正圧に交互に変動
させるコークス炉の炉内圧力変動方法である。
In the second method, a gas supply / exhaust device including a blower, a piping system, and a plurality of valves for switching a piping system is used after the carbonization chamber for repairing the furnace wall is emptied and then closed. First, the piping system is set to a gas supply state by opening and closing the plurality of valves, gas is supplied to the carbonization chamber to make the carbonization chamber positive pressure, and then, the opening and closing of the plurality of valves is changed to discharge the gas from the piping system. This is a coke oven pressure fluctuation method in which the pressure in the coking chamber is alternately changed to a negative pressure and a positive pressure by setting a state and discharging the gas in the coking chamber to make the coking chamber a negative pressure.

【0015】第3の方法は、炉壁の補修に係る炭化室を
空にした後、密閉状態とし、送風機によりガスを前記炭
化室に供給して炭化室を正圧とし、次に、炭化室をガイ
ド車集塵ダクトに連通して負圧にすることにより炭化室
の圧力を負圧と正圧に交互に変動させるコークス炉の炉
内圧力変動方法である。
[0015] A third method is to empty the carbonization chamber for repairing the furnace wall, then close the chamber, and supply a gas to the carbonization chamber with a blower to make the carbonization chamber positive pressure. This is a method for fluctuating the pressure in the coke oven alternately between the negative pressure and the positive pressure by making the pressure in the coking chamber alternately negative and positive by communicating with the guide vehicle dust collection duct.

【0016】第4の方法は、炉壁の補修に係る炭化室を
空にした後、密閉状態とし、シリンダーとピストンから
なる吸排気装置により前記炭化室に給気し、炭化室を正
圧とし、次に、前記吸排気装置により前記炭化室のガス
を吸引し、炭化室を負圧にすることにより炭化室の圧力
を正圧と負圧に交互に変動させることを特徴とするコー
クス炉の炉内圧力変動方法である。
In the fourth method, the carbonization chamber for repairing the furnace wall is emptied and then closed, and the carbonization chamber is supplied with air by a suction / exhaust device comprising a cylinder and a piston, and the carbonization chamber is set to a positive pressure. Then, the gas in the coking chamber is sucked by the suction / exhaust device, and the pressure in the coking chamber is alternately changed to a positive pressure and a negative pressure by setting the coking chamber to a negative pressure. This is a furnace pressure fluctuation method.

【0017】「作用」 第1の方法:燃焼室のウエストバルブを開き、燃焼室を
煙道に連通させると、燃焼室のガスが煙道に吸引されて
燃焼室内は負圧になる。また、燃焼室のウエストバルブ
を閉じると、燃焼室のガスの吸引は中止される。この状
態で、Cガス供給管から燃焼室内に水蒸気を吹き込む
と、燃焼室の高温雰囲気により水蒸気が膨張して燃焼室
内は正圧になる。これを交互に繰り返すことにより、燃
焼室内圧力と炭化室内圧力の差を交互に正負に変動させ
ることができる。
[Operation] First method: When the waist valve of the combustion chamber is opened and the combustion chamber is communicated with the flue, the gas in the combustion chamber is sucked into the flue and the combustion chamber becomes negative pressure. When the waist valve of the combustion chamber is closed, the suction of the gas in the combustion chamber is stopped. In this state, when steam is blown into the combustion chamber from the C gas supply pipe, the steam expands due to the high temperature atmosphere in the combustion chamber, and the combustion chamber becomes positive pressure. By repeating this alternately, the difference between the pressure in the combustion chamber and the pressure in the carbonization chamber can be changed positively and negatively alternately.

【0018】第2の方法:弁の開閉により配管系をガス
供給状態とし、送風機によりガスを炭化室に供給する
と、炭化室内は正圧となる。次に、弁の開閉を変え配管
系をガス排出状態とし、送風機によりガスを炭化室から
排気すると、炭化室内は負圧となる。これを交互に繰り
返すことにより、燃焼室内圧力と炭化室内圧力の差を交
互に正負に変動させることができる。
Second method: When the piping system is set to a gas supply state by opening and closing a valve, and gas is supplied to the coking chamber by a blower, the pressure in the coking chamber becomes positive. Next, by changing the opening and closing of the valve so that the piping system is in a gas discharging state and the gas is exhausted from the carbonizing chamber by the blower, the pressure in the carbonizing chamber becomes negative. By repeating this alternately, the difference between the pressure in the combustion chamber and the pressure in the carbonization chamber can be changed positively and negatively alternately.

【0019】第3の方法:送風機によりガスを炭化室に
供給すると、炭化室内は正圧となる。次に、炭化室をガ
イド車集塵ダクトに連通すると、炭化室内のガスが集塵
ダクトに吸引され、炭化室内は負圧となる。これを交互
に繰り返すことにより、燃焼室内圧力と炭化室内圧力の
差を交互に正負に変動させることができる。
Third method: When gas is supplied to the coking chamber by a blower, the pressure in the coking chamber becomes positive. Next, when the carbonization chamber communicates with the guide vehicle dust collection duct, gas in the carbonization chamber is sucked into the dust collection duct, and the pressure in the carbonization chamber becomes negative. By repeating this alternately, the difference between the pressure in the combustion chamber and the pressure in the carbonization chamber can be changed positively and negatively alternately.

【0020】第4の方法:吸排気装置のピストンを前進
させてシリンダー内のガスを炭化室に供給すると、炭化
室は正圧となる。次に、吸排気装置のピストンを後退さ
せて炭化室内のガスをシリンダー内に吸引すると、炭化
室は負圧となる。これを交互に繰り返すことにより、燃
焼室内圧力と炭化室内圧力の差を交互に正負に変動させ
ることができる。
Fourth method: When the gas in the cylinder is supplied to the carbonization chamber by moving the piston of the intake / exhaust device forward, the carbonization chamber becomes positive pressure. Next, when the gas in the carbonization chamber is sucked into the cylinder by retracting the piston of the intake and exhaust device, the pressure in the carbonization chamber becomes negative. By repeating this alternately, the difference between the pressure in the combustion chamber and the pressure in the carbonization chamber can be changed positively and negatively alternately.

【0021】[0021]

【発明の実施の形態】本発明の実施の形態を図面に基づ
いて以下に説明する。
Embodiments of the present invention will be described below with reference to the drawings.

【0022】第1の方法の実施の形態を図1を参照して
次に説明する。図1は、本発明の第1の方法の説明図で
ある。この図は、燃焼室の断面と炭化室の断面の両方を
合わせて示している。燃焼室2は、複数の区画21に分
けられており、この区画21の中央に仕切壁22が燃焼
室の底部から立設され、その上端と燃焼室2の天井部と
の間は開口となっている。区画21の一方でCガス等の
燃料の燃焼により生じた燃焼ガス9は、仕切壁22の一
方側を上昇し、上方開口で反転して仕切壁22の他方側
を下降し、蓄熱室30→ソールフリュー31→ウエスト
バルブ32を経て煙道33に吸引される。一方、燃焼室
2の下方には、Cガス供給管40が設けられており、こ
のCガス供給管40に複数の分岐管41が立設され、分
岐管41の上端部が区画21の底部に突出している。そ
して、分岐管41を介して燃焼室の各区画21にCガス
を供給するようになっている。本方法を実施するため
に、Cガス供給管40に水蒸気供給管42を接続し、そ
の途中に弁43を設けている。
An embodiment of the first method will be described next with reference to FIG. FIG. 1 is an explanatory diagram of a first method of the present invention. This figure shows both the cross section of the combustion chamber and the cross section of the carbonization chamber together. The combustion chamber 2 is divided into a plurality of sections 21, and a partition wall 22 is provided upright from the bottom of the combustion chamber at the center of the section 21, and an opening is formed between the upper end thereof and the ceiling of the combustion chamber 2. ing. The combustion gas 9 generated by the combustion of the fuel such as the C gas in one of the sections 21 rises on one side of the partition wall 22, reverses at the upper opening, and descends on the other side of the partition wall 22, and the heat storage chamber 30 → Sole flue 31 is sucked into the flue 33 via the waist valve 32. On the other hand, a C gas supply pipe 40 is provided below the combustion chamber 2, and a plurality of branch pipes 41 are erected on the C gas supply pipe 40, and the upper end of the branch pipe 41 is located at the bottom of the section 21. It is protruding. Then, C gas is supplied to each section 21 of the combustion chamber via the branch pipe 41. In order to carry out this method, a steam supply pipe 42 is connected to a C gas supply pipe 40, and a valve 43 is provided on the way.

【0023】第1の方法は、次のように行われる。 (1)炉壁を補修する炭化室1を空窯とし、炭化室1の
両側の炉蓋、装炭口11の装入蓋5を閉じ、炭化室1と
連通する上昇管12とドライメーン14の間のガスの流
通を遮断する水封弁13を閉じる。また、このとき、炭
化室1の両側の燃焼室2の燃焼を中止し、ウエストバル
ブ32を閉じる。 (2)上昇管12の頂部のガス放散弁15を開け、装入
蓋5に設けた図示しない供給管からSiCl4 含有ガスを炭
化室1内に供給し、炭化室1内の空気と置換し、ガス放
散弁15とSiCl4 含有ガス供給管の弁(図示せず)を閉
じて、炭化室1を密閉状態とする。 (3)ウエストバルブ32を開ける。燃焼室2のガス
が、蓄熱室30→ソールフリュー31→ウエストバルブ
32を介して煙道33に吸引され、燃焼室1内は約−2
0mmAqとなる。この状態を一定時間継続する。 (4)ウエストバルブを閉じるとともに、水蒸気供給管
42の弁43を開き、水蒸気をCガス供給管40→分岐
管41を通して燃焼室1内に供給し、燃焼室内圧力が、
約+50mmAqとなったら、この圧力状態を一定時間
継続し、その後水蒸気の供給を中止する。 (5)上記(3)および(4)を一定回数繰り返す。
The first method is performed as follows. (1) The coking chamber 1 for repairing the furnace wall is an empty kiln, the furnace lids on both sides of the coking chamber 1, the charging lid 5 of the coal charging port 11 are closed, and the riser pipe 12 and the dry main 14 communicating with the coking chamber 1. The water seal valve 13 for shutting off the gas flow during the period is closed. At this time, the combustion in the combustion chambers 2 on both sides of the carbonization chamber 1 is stopped, and the waist valve 32 is closed. (2) The gas release valve 15 at the top of the riser pipe 12 is opened, and a SiCl 4 -containing gas is supplied into the carbonization chamber 1 from a supply pipe (not shown) provided in the charging lid 5 to replace the air in the carbonization chamber 1. Then, the gas release valve 15 and a valve (not shown) of the SiCl 4 -containing gas supply pipe are closed, and the carbonization chamber 1 is closed. (3) Open the waist valve 32. The gas in the combustion chamber 2 is sucked into the flue 33 via the heat storage chamber 30 → the sole flute 31 → the waist valve 32, and the inside of the combustion chamber 1 is about −2.
0 mmAq. This state is continued for a fixed time. (4) With the waist valve closed, the valve 43 of the steam supply pipe 42 is opened, and steam is supplied into the combustion chamber 1 through the C gas supply pipe 40 → the branch pipe 41.
When the pressure reaches about +50 mmAq, this pressure state is maintained for a certain period of time, and then the supply of steam is stopped. (5) The above (3) and (4) are repeated a fixed number of times.

【0024】第2の方法の実施の形態を図2を参照して
次に説明する。図2は、本発明の第2の方法の説明図で
ある。この図で炭化室1は断面図で示している。50は
炉頂に設けられた送風機、51は吸引管、52は吸引管
51の途中に設けられた弁、53はガス発生器、54は
ガス供給管、55はガス供給管の途中に設けられた弁で
ある。56は第1の吐出管、57は第1の吐出管の途中
に設けられた弁、58は弁57の下方の第1の吐出管5
6から分岐した第2の吐出管、59は第2の吐出管58
の途中に設けられた弁、第2の吐出管58の先端は装入
蓋5を通して炭化室1内に突出している。なお、炭化室
1の内圧の変動範囲は、水封弁13の水位が50mmで
あるので、−40〜+40mmAqとする必要がある。
An embodiment of the second method will be described next with reference to FIG. FIG. 2 is an explanatory diagram of the second method of the present invention. In this figure, the carbonization chamber 1 is shown in a sectional view. 50 is a blower provided on the furnace top, 51 is a suction pipe, 52 is a valve provided in the middle of the suction pipe 51, 53 is a gas generator, 54 is a gas supply pipe, and 55 is provided in the middle of the gas supply pipe. It is a valve. 56 is a first discharge pipe, 57 is a valve provided in the middle of the first discharge pipe, and 58 is a first discharge pipe 5 below the valve 57.
A second discharge pipe branched from 6, 59 is a second discharge pipe 58.
The tip of the second discharge pipe 58 protrudes into the carbonization chamber 1 through the charging lid 5. In addition, the fluctuation range of the internal pressure of the carbonization chamber 1 needs to be −40 to +40 mmAq because the water level of the water seal valve 13 is 50 mm.

【0025】第2の方法は、次のように行われる。 (1)炉壁を補修する炭化室1を空窯とし、炭化室1の
両側の炉蓋、装炭口11の装入蓋5を閉じ、炭化室1と
連通する上昇管12とドライメーン14の間のガスの流
通を遮断する水封弁13を閉じる。 (2)弁52、57を閉、弁55、59を開、ガス放散
弁12を開とし、送風機50を運転してガス発生器53
で発生したSiCl4 含有ガスを、ガス供給管54→吸引管
51→送風機50→第1の吐出管56→第2の吐出管を
経由して炭化室1に供給し、炭化室内の空気と置換す
る。置換が終了したらガス放散弁15を閉じて炭化室1
を密閉状態とする。 (3)送風機50を運転し、炭化室1の内圧が、+40
mmAqとなったら送風機の運転を停止し、この状態を
一定時間継続する。 (4)弁55、59を閉、弁52、57を開とし、送風
機50を運転し、炭化室1内のガスを第2の吐出管58
→吸引管51→送風機50→第1の吐出管56を経由し
て大気に放散し、炭化室1の内圧が−40mmAqとな
ったら送風機50の運転を停止し、この状態を一定時間
継続する。 (5)上記(3)および(4)を一定回数繰り返す。
The second method is performed as follows. (1) The coking chamber 1 for repairing the furnace wall is an empty kiln, the furnace lids on both sides of the coking chamber 1, the charging lid 5 of the coal charging port 11 are closed, and the riser pipe 12 and the dry main 14 communicating with the coking chamber 1. The water seal valve 13 for shutting off the gas flow during the period is closed. (2) The valves 52 and 57 are closed, the valves 55 and 59 are opened, the gas release valve 12 is opened, and the blower 50 is operated to operate the gas generator 53.
The in generated SiCl 4 containing gas, a gas supply pipe 54 → the suction pipe 51 → the blower 50 → first discharge pipe 56 → via the second discharge pipe is supplied to the carbonization chamber 1, substitution with air carbonization chamber I do. When the replacement is completed, the gas release valve 15 is closed and the carbonization chamber 1
Is closed. (3) The blower 50 is operated, and the internal pressure of the carbonization chamber 1 is increased by +40.
When the pressure reaches mmAq, the operation of the blower is stopped, and this state is continued for a certain time. (4) The valves 55 and 59 are closed, the valves 52 and 57 are opened, the blower 50 is operated, and the gas in the carbonization chamber 1 is discharged to the second discharge pipe 58.
→ Suction pipe 51 → Blower 50 → Dissipates to the atmosphere via first discharge pipe 56. When the internal pressure of carbonization chamber 1 becomes −40 mmAq, operation of blower 50 is stopped and this state is continued for a certain period of time. (5) The above (3) and (4) are repeated a fixed number of times.

【0026】第3の方法の実施の形態を図3を参照して
次に説明する。図3は、本発明の第3の方法の説明図で
ある。この図で炭化室1は断面図で示している。60は
送風機、53はガス発生機、54は吸引管、61は吐出
管、62は吐出管61の途中に設けられた弁である。吐
出管61の先端部は、装入蓋5を通して炭化室1内に突
出している。63はガイド車集塵ダクト、64は集塵ダ
クト63に取付られた吸引枝管、65は吸引枝管64の
途中に設けられた弁、66は吸引枝管64にフランジ接
合された配管である。配管66の先端部は装入蓋5を通
して炭化室1内に突出している。
An embodiment of the third method will now be described with reference to FIG. FIG. 3 is an explanatory diagram of the third method of the present invention. In this figure, the carbonization chamber 1 is shown in a sectional view. Reference numeral 60 denotes a blower, 53 denotes a gas generator, 54 denotes a suction pipe, 61 denotes a discharge pipe, and 62 denotes a valve provided in the discharge pipe 61. The distal end of the discharge pipe 61 protrudes into the carbonization chamber 1 through the charging lid 5. 63 is a guide car dust collecting duct, 64 is a suction branch pipe attached to the dust collecting duct 63, 65 is a valve provided in the middle of the suction branch pipe 64, and 66 is a pipe flanged to the suction branch pipe 64. . The tip of the pipe 66 projects into the carbonization chamber 1 through the charging lid 5.

【0027】第3の方法は、次のように行われる。 (1)炉壁を補修する炭化室1を空窯とし、炭化室1の
両側の炉蓋、装炭口11の装入蓋5を閉じ、炭化室1と
連通する上昇管12とドライメーン14の間のガスの流
通を遮断する水封弁13を閉じる。 (2)弁62を開、ガス放散弁15を開として送風機6
0を運転し、ガス発生機53で発生したSiCl4 含有ガス
を、吸引管54→送風機60→吐出管61を経由して炭
化室1に供給し、炭化室内の空気と置換する。置換が終
了したらガス放散弁15を閉じて炭化室1を密閉状態と
する。 (3)送風機60を運転し、炭化室1の内圧が+40m
mAqとなったら、送風機60の運転を停止し、この状
態を一定時間継続する。 (4)弁65を開とし、炭化室1内のガスを配管66→
吸引枝管64→集塵ダクト63を経由して吸引させ、炭
化室1の内圧が、−40mmAqとなったら、弁65を
閉とし、この状態を一定時間継続する。 (5)上記(3)および(4)を一定回数繰り返す。
The third method is performed as follows. (1) The coking chamber 1 for repairing the furnace wall is an empty kiln, the furnace lids on both sides of the coking chamber 1, the charging lid 5 of the coal charging port 11 are closed, and the riser pipe 12 and the dry main 14 communicating with the coking chamber 1. The water seal valve 13 for shutting off the gas flow during the period is closed. (2) Open the valve 62 and open the gas release valve 15 to
In operation 0, the SiCl 4 -containing gas generated by the gas generator 53 is supplied to the carbonization chamber 1 via the suction pipe 54 → the blower 60 → the discharge pipe 61 to replace the air in the carbonization chamber. When the replacement is completed, the gas release valve 15 is closed, and the carbonization chamber 1 is closed. (3) The blower 60 is operated, and the internal pressure of the carbonization chamber 1 is +40 m.
When mAq is reached, the operation of the blower 60 is stopped, and this state is continued for a certain period of time. (4) Open the valve 65 and supply the gas in the carbonization chamber 1 to the pipe 66 →
The suction is performed through the suction branch pipe 64 → the dust collection duct 63, and when the internal pressure of the carbonization chamber 1 becomes −40 mmAq, the valve 65 is closed, and this state is continued for a certain time. (5) The above (3) and (4) are repeated a fixed number of times.

【0028】第4の方法の実施の形態を図4を参照し
て、次に説明する。図4は、本発明の第4の方法の説明
図である。この図で炭化室1は、断面図で示している。
吸排気装置70は、シリンダー71とピストン73から
なり、ピストン73を後退させることによりガスをシリ
ンダー71内に吸引し、ピストン73を前進させること
により先に吸引したシリンダー71内のガスを排出する
ものである。72はシリンダー71の後端に設けられた
吸排気口、75はシリンダー71の前端に接続された吸
排気管で、その先端は装入蓋5を通して炭化室1内に突
出している。74はシリンダーロッドで、図示しない往
復動装置に連結されている。
An embodiment of the fourth method will be described next with reference to FIG. FIG. 4 is an explanatory diagram of the fourth method of the present invention. In this figure, the carbonization chamber 1 is shown in a sectional view.
The intake / exhaust device 70 is composed of a cylinder 71 and a piston 73, in which gas is sucked into the cylinder 71 by retracting the piston 73, and exhausted in the cylinder 71 by moving the piston 73 forward. It is. Reference numeral 72 denotes an intake / exhaust port provided at the rear end of the cylinder 71, and reference numeral 75 denotes an intake / exhaust pipe connected to the front end of the cylinder 71, the tip of which protrudes into the carbonization chamber 1 through the charging lid 5. A cylinder rod 74 is connected to a reciprocating device (not shown).

【0029】第4の方法は、次のように行われる。 (1)炉壁を補修する炭化室1を空窯とし、炭化室1の
両側の炉蓋、装炭口11の装入蓋5を閉じ、炭化室1と
連通する上昇管12とドライメーン14の間のガスの流
通を遮断する水封弁13を閉じる。 (2)ガス放散弁15を開とし、図示しないガス供給装
置によりSiCl4 含有ガスを炭化室1に供給し、炭化室1
内の空気と置換する。置換が終了したらガス放散弁15
を閉じて炭化室1を密閉状態とする。 (3)吸排気装置70のピストン73を前進させてシリ
ンダー71内のガスを炭化室1に供給し、炭化室1の内
圧が+40mmAqとなったら供給を中止し、この状態
を一定時間継続する。 (4)吸排気装置70のピストン73を後退させて炭化
室1内のガスをシリンダー71内に吸引し、炭化室1の
内圧が−40mmAqとなったら、吸引を中止し、この
状態を一定時間継続する。 (5)上記(3)および(4)を一定回数繰り返す。
The fourth method is performed as follows. (1) The coking chamber 1 for repairing the furnace wall is an empty kiln, the furnace lids on both sides of the coking chamber 1, the charging lid 5 of the coal charging port 11 are closed, and the riser pipe 12 and the dry main 14 communicating with the coking chamber 1. The water seal valve 13 for shutting off the gas flow during the period is closed. (2) The gas release valve 15 is opened, and a SiCl 4 -containing gas is supplied to the coking chamber 1 by a gas supply device (not shown).
Replace with air inside. When the replacement is completed, gas release valve 15
Is closed to put the carbonization chamber 1 in a sealed state. (3) The piston 73 of the intake / exhaust device 70 is advanced to supply the gas in the cylinder 71 to the coking chamber 1, and when the internal pressure of the coking chamber 1 becomes +40 mmAq, the supply is stopped, and this state is continued for a certain time. (4) The piston 73 of the intake / exhaust device 70 is retracted to suck the gas in the carbonization chamber 1 into the cylinder 71. When the internal pressure of the carbonization chamber 1 becomes −40 mmAq, the suction is stopped, and this state is maintained for a certain period of time. continue. (5) The above (3) and (4) are repeated a fixed number of times.

【0030】[0030]

【発明の効果】本発明の方法によれば、燃焼室内圧力ま
たは炭化室内圧力を正負圧に交互に変動させることがで
きる。これにより炉壁の貫通損傷部に炭化室側からSiCl
4 含有ガスを、燃焼室側から水蒸気を浸透させ、貫通損
傷部にSiO2の充填を促進させることができる。
According to the method of the present invention, the pressure in the combustion chamber or the pressure in the carbonization chamber can be changed alternately between positive and negative pressures. As a result, the SiCl
(4) The vapor containing gas can permeate the vapor from the combustion chamber side to promote the filling of the penetration damage portion with SiO 2 .

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

【図1】本発明の第1の方法の説明図である。FIG. 1 is an explanatory diagram of a first method of the present invention.

【図2】本発明の第2の方法の説明図である。FIG. 2 is an explanatory diagram of a second method of the present invention.

【図3】本発明の第3の方法の説明図である。FIG. 3 is an explanatory diagram of a third method of the present invention.

【図4】本発明の第4の方法の説明図である。FIG. 4 is an explanatory diagram of a fourth method of the present invention.

【図5】SiCl4 含有ガスと燃焼ガス中の水蒸気によるコ
ークス炉の炉壁補修の説明図である。
FIG. 5 is an explanatory diagram of furnace wall repair of a coke oven using a SiCl 4 -containing gas and steam in a combustion gas.

【符号の説明】[Explanation of symbols]

1 炭化室 2 燃焼室 3 炉壁 5 装入蓋 6、7 貫通損傷部 12 上昇管 13 水封弁 14 ドライメーン 15 ガス放散弁 32 ウエストバルブ 33 煙道 40 Cガス供給管 42 水蒸気供給管 50 送風機 51,54,56,58 配管系 52,55,57,58 弁 53 ガス発生機 60 送風機 63 集塵ダクト 70 吸排気装置 71 シリンダー 73 ピストン 74 シリンダーロッド 75 吸排気管 DESCRIPTION OF SYMBOLS 1 Carbonization chamber 2 Combustion chamber 3 Furnace wall 5 Charging lid 6, 7 Penetration damaged part 12 Rise pipe 13 Water seal valve 14 Dry main 15 Gas release valve 32 West valve 33 Flue 40 C gas supply pipe 42 Steam supply pipe 50 Blower 51, 54, 56, 58 Piping system 52, 55, 57, 58 Valve 53 Gas generator 60 Blower 63 Dust collection duct 70 Suction and exhaust device 71 Cylinder 73 Piston 74 Cylinder rod 75 Suction and exhaust pipe

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 炉壁の補修に係わる燃焼室の燃焼を中止
した後、該燃焼室のウエストバルブを開き、前記燃焼室
を煙道に連通させ燃焼室を負圧にし、次に、前記ウエス
トバルブを閉じ、Cガス供給管を介して前記燃焼室に水
蒸気を吹込み、燃焼室を正圧にすることにより燃焼室の
圧力を負圧と正圧に交互に変動させることを特徴とする
コークス炉の炉内圧力変動方法。
After stopping combustion in a combustion chamber related to repair of a furnace wall, a waist valve of the combustion chamber is opened, the combustion chamber is connected to a flue, and a pressure in the combustion chamber is reduced. Coke characterized in that the valve is closed, steam is blown into the combustion chamber via a C gas supply pipe, and the pressure in the combustion chamber is alternately changed to negative pressure and positive pressure by making the combustion chamber positive pressure. How to change the pressure inside the furnace.
【請求項2】 炉壁の補修に係る炭化室を空にした後、
密閉状態とし、送風機、配管系および配管系を切り替え
る複数の弁からなるガス給排気装置を使用して、最初
に、前記複数の弁の開閉により配管系をガス供給状態と
し、ガスを前記炭化室に供給して炭化室を正圧とし、次
に、前記複数の弁の開閉を変え配管系をガス排出状態と
し、炭化室のガスを排出して炭化室を負圧にすることに
より炭化室の圧力を負圧と正圧に交互に変動させること
を特徴とするコークス炉の炉内圧力変動方法。
2. After emptying the carbonization chamber for repairing the furnace wall,
Using a gas supply / exhaust device comprising a plurality of valves for switching between a blower, a piping system and a piping system in a closed state, first, the piping system is brought into a gas supply state by opening and closing the plurality of valves, and the gas is supplied to the carbonization chamber. To a positive pressure in the carbonization chamber, and then change the opening and closing of the plurality of valves to bring the piping system into a gas discharge state, and discharge the gas in the carbonization chamber to make the carbonization chamber a negative pressure, thereby reducing the pressure in the carbonization chamber. A method for fluctuating pressure in a coke oven, wherein the pressure is fluctuated alternately between negative pressure and positive pressure.
【請求項3】 炉壁の補修に係る炭化室を空にした後、
密閉状態とし、送風機によりガスを前記炭化室に供給し
て炭化室を正圧とし、次に、炭化室をガイド車集塵ダク
トに連通して負圧にすることにより炭化室の圧力を負圧
と正圧に交互に変動させることを特徴とするコークス炉
の炉内圧力変動方法。
3. After emptying the carbonization chamber for repairing the furnace wall,
In a closed state, gas is supplied to the carbonization chamber by a blower to make the carbonization chamber positive pressure, and then the carbonization chamber is communicated with the guide vehicle dust collecting duct to make it negative pressure, thereby reducing the pressure of the carbonization chamber to negative pressure. Pressure fluctuation method for a coke oven characterized by alternately fluctuating pressure and positive pressure.
【請求項4】 炉壁の補修に係る炭化室を空にした後、
密閉状態とし、シリンダーとピストンからなる吸排気装
置により前記炭化室に給気し、炭化室を正圧とし、次
に、前記吸排気装置により前記炭化室のガスを吸引し、
炭化室を負圧にすることにより炭化室の圧力を正圧と負
圧に交互に変動させることを特徴とするコークス炉の炉
内圧力変動方法。
4. After emptying the carbonization chamber for repairing the furnace wall,
In a closed state, air is supplied to the carbonization chamber by a suction and exhaust device including a cylinder and a piston, the carbonization chamber is set to a positive pressure, and then the gas in the carbonization chamber is suctioned by the suction and exhaust device.
A method of fluctuating pressure in a coke oven, wherein the pressure of the coking chamber is alternately changed to a positive pressure and a negative pressure by setting the coking chamber to a negative pressure.
JP34864196A 1996-12-26 1996-12-26 Change of pressure in furnace of coke furnace Pending JPH10183131A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP34864196A JPH10183131A (en) 1996-12-26 1996-12-26 Change of pressure in furnace of coke furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP34864196A JPH10183131A (en) 1996-12-26 1996-12-26 Change of pressure in furnace of coke furnace

Publications (1)

Publication Number Publication Date
JPH10183131A true JPH10183131A (en) 1998-07-14

Family

ID=18398372

Family Applications (1)

Application Number Title Priority Date Filing Date
JP34864196A Pending JPH10183131A (en) 1996-12-26 1996-12-26 Change of pressure in furnace of coke furnace

Country Status (1)

Country Link
JP (1) JPH10183131A (en)

Similar Documents

Publication Publication Date Title
CN101907298B (en) Hot repair method of port tongue arch of coal-burning glass furnace
JPH10183131A (en) Change of pressure in furnace of coke furnace
CN203024566U (en) Energy-saving and environment-protecting high wind temperature cupola system device
CN204064005U (en) Regenerative cycles device in Gas heating furnace high-temperature burns carbon distribution device
EP0905212B1 (en) Method for repairing and/or reinforcing a bulkhead for a bulkhead type heat exchanger
JP3687242B2 (en) Coke oven wall repair method
JPH10183126A (en) Discharge of generated gas when repairing furnace wall of coke furnace
CN213179429U (en) High-temperature kiln for firing refractory bricks
JPH10183127A (en) Discharge of generated gas when repairing furnace wall of coke furnace
JP3209087B2 (en) Repair method and reinforcement method of silica stone brick wall of kiln
CN202576337U (en) Device for cleaning sundries in vertical flame path of coke oven by negative pressure
CN104197733B (en) Regenerative cycles device in Gas heating furnace high-temperature burns carbon distribution device and technique
JP3209062B2 (en) Method for repairing and / or strengthening a partition wall of a partition type heat exchanger
JPH10183130A (en) Treatment of combustion exhaust gas when repairing furnace wall of coke furnace
CN103063011B (en) Energy-saving environment-friendly high-blast-temperature cupola system equipment
CN111879133A (en) Clean carbon product roasting furnace
JP4023027B2 (en) How to repair the wall of a bulkhead furnace
JP4035033B2 (en) Coke oven carbonization chamber heat shutoff method and heat shutoff device
CN205893098U (en) Porous internal combustion type shaft kiln
CN220867460U (en) Hot-blast stove system and exhaust gas emission device thereof
CN209741011U (en) Device for prolonging service life of high-temperature shaft kiln
CN208398100U (en) Ultralow concentration gas dual oxide device
JP2002201477A (en) Method for repairing coke oven opening
CN205825691U (en) Vacuum combustion furnace
CN2514283Y (en) Burning-in kiln using gas more tran needed of blast furnace