JPH1036850A - Dry-process coke quencher - Google Patents
Dry-process coke quencherInfo
- Publication number
- JPH1036850A JPH1036850A JP18939296A JP18939296A JPH1036850A JP H1036850 A JPH1036850 A JP H1036850A JP 18939296 A JP18939296 A JP 18939296A JP 18939296 A JP18939296 A JP 18939296A JP H1036850 A JPH1036850 A JP H1036850A
- Authority
- JP
- Japan
- Prior art keywords
- gas
- dust
- boiler
- cooling tower
- tower
- 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
Links
Landscapes
- Coke Industry (AREA)
Abstract
Description
【０００１】[0001]
【発明の属する技術分野】本発明は、コークス乾式消火
設備に関し、詳しくは、該コークス乾式消火設備で発生
した余剰ガスを回収するに際し、該余剰ガスが含有する
ダストを迅速、且つトラブルなく処理する技術に係わ
る。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a coke dry fire extinguishing system, and more particularly, to recovering surplus gas generated in a coke dry fire extinguishing system, quickly and without trouble in dust contained in the surplus gas. Related to technology.
【０００２】[0002]
【従来の技術】一般に、室炉式コークス炉の炭化室から
押出された赤熱コークスを消火する設備として、図３に
示すようなコークス乾式消火設備（以下、ＣＤＱとい
う）が知られている。それは、冷却塔１内に装入された
赤熱コークス２を、下方からブロア５を介して吹き込ん
だ不活性ガス４で冷却し、消火したコークス３を該冷却
塔１の下部より塔外へ排出するものである。その際、吹
き込まれた不活性ガス４は、赤熱コークス２と熱交換し
て昇温し、高温排出不活性ガス（通常８００℃前後）３
０となって、上記冷却塔１の上部より排出される。この
高温排出不活性ガス３０は、次いで沈降室タイプの簡単
な除塵器６で粗粒ダストを除き、その顕熱は排熱回収用
ボイラ８（以下、ボイラという）で水蒸気として回収さ
れる。次いで、該ボイラ８との熱交換で降温した低温排
出不活性ガス（通常２００℃前後）３１は、除塵器（一
般に、サイクロンを使用）１０に導かれて細粒ダストを
除き、再び冷却塔１への不活性ガスとして循環使用され
る。2. Description of the Related Art Generally, a coke dry fire extinguishing system (hereinafter referred to as CDQ) as shown in FIG. 3 is known as a system for extinguishing red hot coke extruded from a carbonization chamber of a coke oven furnace. That is, the red-hot coke 2 charged in the cooling tower 1 is cooled by an inert gas 4 blown from below through a blower 5, and the extinguished coke 3 is discharged from the lower part of the cooling tower 1 to the outside of the tower. Things. At this time, the injected inert gas 4 exchanges heat with the red hot coke 2 to increase the temperature, and the high temperature discharged inert gas (normally around 800 ° C.) 3
It becomes 0 and is discharged from the upper part of the cooling tower 1. The high-temperature discharged inert gas 30 is then subjected to removal of coarse dust by a simple settling chamber type dust remover 6, and its sensible heat is recovered as steam in a waste heat recovery boiler 8 (hereinafter referred to as a boiler). Next, the low-temperature discharge inert gas (usually around 200 ° C.) 31 whose temperature has been lowered by heat exchange with the boiler 8 is guided to a dust remover (generally using a cyclone) 10 to remove fine-grained dust, and again to the cooling tower 1. Circulated as inert gas to
【０００３】ところで、上記冷却塔では、赤熱コークス
の消火処理に際し、水素（Ｈ2 ）ガスや一酸化炭素ガス
（ＣＯ）が発生する。このＨ2 やＣＯ等の可燃ガスを含
む前記高温の排出不活性ガス３０は、爆発の危険がある
ので、冷却塔からの排出直後に、そのガス組成の変化に
応じ、希釈空気用ブロア２７に接続した空気配管２８を
介して空気を吹込み、希釈されるようになっている。そ
のため、該冷却塔へ戻るガスは、順次増量することにな
るが、従来は、その増量分を余剰ガス３２として放散管
１１の先端で燃焼させつつ、大気中に放散していた。し
かし、この余剰ガス３２の大気放散はエネルギーの損失
となるので、最近は、可燃ガスとして回収し、燃料ガス
として利用されるようになっている。この余剰ガス３２
の回収・利用に際しては、前記サイクロン１０を通った
低温排出不活性ガス３１にまだ微細粒のダストが相当含
まれているので、後述する余剰ガス３２の回収経路内
（図示せず）にそれらダストが堆積し、回収作業でトラ
ブルになるという問題があった。従って、該余剰ガス３
２の回収時には、ガス中のかかる微細粒ダストを除塵す
る必要があった。In the cooling tower, hydrogen (H 2 ) gas and carbon monoxide gas (CO) are generated when extinguishing red hot coke. Since the high-temperature discharged inert gas 30 containing a combustible gas such as H 2 or CO has a risk of explosion, immediately after being discharged from the cooling tower, the inert gas 30 is supplied to the dilution air blower 27 in accordance with a change in the gas composition. Air is blown through the connected air pipe 28 to be diluted. For this reason, the amount of gas returning to the cooling tower is sequentially increased. Conventionally, the increased amount is burned as excess gas 32 at the tip of the diffusion tube 11 and emitted into the atmosphere. However, since the emission of the surplus gas 32 to the atmosphere causes a loss of energy, it has recently been recovered as a combustible gas and used as a fuel gas. This surplus gas 32
At the time of recovery / utilization of the gas, since the low-temperature discharge inert gas 31 that has passed through the cyclone 10 still contains considerable fine-grain dust, the dust is contained in a recovery path (not shown) of the surplus gas 32 described later. Has been deposited, causing a problem in the recovery operation. Therefore, the surplus gas 3
At the time of recovery of 2, it was necessary to remove such fine-grain dust in the gas.
【０００４】そこで、特公平５−５４７８９号公報は、
ＣＤＱの余剰ガス回収方法を提案した。それは、図２に
示すように、ＣＤＱの循環ガス配管（図示せず）から循
環ガスの一部を吸引ブロア２１で余剰ガス３２として吸
引し、それをバッグ・フィルタ１３に導いて、含有する
微細粒ダストを除去してから、余剰ガス回収用配管１４
を介してガス本管１５に回収する方法である。つまり、
バッグ・フィルタ１３に吸引する余剰ガス３２は、その
温度低下によりガス中の水分が凝縮、ドレン化し、さら
に該ドレンがダストと混合、結合して管を閉塞し、回収
作業ができなくなるが、この問題を、ガス配管１２やバ
ッグ・フィルタ１３の本体にスチーム・トレース２２を
設け、吸引した余剰ガス３２を加熱しての温度低下を抑
え、ドレン化を防止すると共に、バッグ・フィルタ１３
のダスト払い落とし用気体３３に対しても加熱器１９を
設け、加熱するようにしたものである。Therefore, Japanese Patent Publication No. 5-54789 discloses that
A surplus gas recovery method for CDQ was proposed. As shown in FIG. 2, a part of the circulating gas is sucked from a CDQ circulating gas pipe (not shown) as excess gas 32 by a suction blower 21 and guided to the bag / filter 13 to contain fine particles. After removing the particulate dust, the excess gas recovery pipe 14
Is collected in the gas main pipe 15 through the main body. That is,
The excess gas 32 sucked into the bag / filter 13 is condensed and drained due to a decrease in the temperature of the gas, and the drain mixes with and binds to the dust to block the pipe, thereby making it impossible to recover the gas. The problem is that the steam trace 22 is provided on the gas pipe 12 and the main body of the bag filter 13 to suppress the temperature drop by heating the sucked excess gas 32, prevent the drainage, and prevent the bag filter 13.
The heater 19 is also provided for the dust removing gas 33 to heat it.
【０００５】しかしながら、特公平５−５４８７９号公
報記載の技術は、バッグ・フィルタ１３で微細粒ダスト
を捕集するまでは良いが、捕集したダストの排出が間欠
的であるためか、排出系配管１６で温度低下が起きる
と、やはりガス中の蒸気が結露、ドレン化して、該ドレ
ンと微細粒ダスト２５とが混合して形成した付着・堆積
物が、排出系を閉塞させるという別の問題が生じた。ま
た、結露した水分は、ガス中に含有する二酸化硫黄（Ｓ
Ｏ2 ）と結合して硫酸を生成し、ダスト２５の排出系配
管内や排出ブロア１７、あるいはその他機器の表面を腐
食させ、閉塞を助長する作用を示した。さらに、腐食が
進行すると、余剰ガス３２の除塵設備全体の寿命を短縮
させる恐れもあった。さらに加えて、特公平５−５４８
７９号公報記載の設備は、大掛かりで建設費が高いこ
と、加熱用蒸気の消費量が大きいこと、多数設置された
各ブロアでの消費電力が大きいこと等の欠点があり、経
済的にも問題があった。[0005] However, the technique described in Japanese Patent Publication No. 5-54879 is good until the fine dust is collected by the bag filter 13, but the collected dust is intermittently discharged. When the temperature of the pipe 16 is lowered, the vapor in the gas is condensed and drained, and another problem is that the deposits and deposits formed by mixing the drain and the fine particle dust 25 block the discharge system. Occurred. In addition, the condensed water contains sulfur dioxide (S) contained in the gas.
Sulfuric acid was generated by combining with O 2 ), which corroded the inside of the discharge system piping of the dust 25, the discharge blower 17, or the surface of other equipment, and showed an effect of promoting clogging. Further, when the corrosion progresses, there is a possibility that the life of the entire dust removing facility for the surplus gas 32 may be shortened. In addition, 5-548
The equipment described in Japanese Patent No. 79 has disadvantages such as large scale and high construction cost, large consumption of heating steam, and large power consumption in each of a large number of blowers. was there.
【０００６】[0006]
【発明が解決しようとする課題】本発明は、かかる事情
を鑑み、余剰ガスの回収を、簡易で、且つ小規模な手段
の利用で、円滑に安定して行えるコークス乾式消火設備
を提供することを目的としている。SUMMARY OF THE INVENTION The present invention has been made in view of the above circumstances, and provides a coke dry fire extinguishing system capable of recovering surplus gas smoothly and stably by using simple and small-scale means. It is an object.
【０００７】[0007]
【課題を解決するための手段】発明者は、上記目的を達
成するため、余分な加熱手段やブロアを使用せずに、対
処することを鋭意研究し、ボイラから排出され、まだ２
００℃の温度を有する前記排出不活性ガスの利用と、余
剰ガス回収経路内の集塵機で捕集したダストの早期除去
とに着眼し、本発明を完成させた。Means for Solving the Problems The inventor has studied diligently to achieve the above object without using an extra heating means or a blower, and has been exhausted from the boiler and still has 2
The present invention was completed by focusing on utilization of the discharged inert gas having a temperature of 00 ° C. and early removal of dust collected by a dust collector in a surplus gas recovery path.
【０００８】すなわち、本発明は、赤熱コークスを保持
する冷却塔と、該冷却塔に冷却用の不活性ガスを送るブ
ロアと、該冷却塔の廃ガスからその顕熱を回収するボイ
ラと、該ボイラを通過した廃ガスの除塵を行う除塵器
と、該除塵器を経た廃ガスを前記冷却塔へ戻す循環路
と、該循環路の上記ブロアから冷却塔までの間で分岐さ
れ可燃ガスとして回収される余剰ガスを集塵するバッグ
・フィルタとからなるコークス乾式消火設備において、
上記バッグ・フィルタの下部にダストを連続的に抜き出
す排出手段を設け、上記ボイラと除塵器との間を結ぶ配
管に、前記排出手段からのダスト搬送管を接続したこと
を特徴とするコークス乾式消火設備である。That is, the present invention provides a cooling tower for holding red hot coke, a blower for sending an inert gas for cooling to the cooling tower, a boiler for recovering sensible heat from waste gas of the cooling tower, and A dust remover that removes dust from the waste gas that has passed through the boiler, a circulation path that returns the waste gas that has passed through the dust remover to the cooling tower, and a branch between the blower and the cooling tower in the circulation path that is collected as combustible gas. Coke dry fire extinguishing system consisting of a bag and a filter that collects excess gas
Coke dry fire extinguishing characterized by providing a discharge means for continuously extracting dust at a lower portion of the bag filter, and connecting a dust transfer pipe from the discharge means to a pipe connecting between the boiler and the dust remover. Equipment.
【０００９】また、本発明は、上記排出手段をスパイラ
ル・コンベアとしたことを特徴とするコークス乾式消火
設備である。本発明では、ＣＤＱを上記のようにしたの
で、特別な加熱手段を設けなくとも、バッグ・フィルタ
を通過する余剰ガス量を従来より増やすことができ、該
ガスの温度降下程度を減少させる。その結果、そこを通
過する余剰ガス中の水分は、結露しないようになり、ト
ラブルなく円滑な余剰ガスの回収が行われるようにな
る。また、捕集ダストは、直ちに前記サイクロンで回収
するので、もし万一ダスト排出系でドレンができても、
多量の付着物や堆積物を形成しないようになる。なお、
余剰ガスの増量は、前記希釈空気の増量で行われる。Further, the present invention is a coke dry fire extinguishing facility, wherein the discharging means is a spiral conveyor. In the present invention, since the CDQ is made as described above, the amount of surplus gas passing through the bag filter can be increased without providing any special heating means, and the degree of temperature drop of the gas is reduced. As a result, the moisture in the surplus gas passing therethrough does not condense, and the surplus gas can be smoothly collected without any trouble. In addition, since the collected dust is immediately collected by the cyclone, even if the dust is generated in the dust discharge system,
It does not form a large amount of deposits and deposits. In addition,
The surplus gas is increased by increasing the dilution air.
【００１０】[0010]
【発明の実施の形態】本発明に係るＣＤＱを図１に示
す。それは、赤熱コークス２を保持する冷却塔１と、該
冷却塔１に冷却用の不活性ガスを送るブロア５と、該冷
却塔１の廃ガスからその顕熱を回収するボイラ８と、該
ボイラ８を通過した廃ガスの除塵を行うサイクロン１０
と、該サイクロン１０を経た廃ガスを前記冷却塔１へ戻
す循環路と、廃ガスの一部を余剰ガス３２として抜き出
す該循環路から分岐した放散管１１と、該放散管１１か
ら分岐し、可燃ガスとして回収される余剰ガス３２を集
塵するバッグ・フィルタ１３とからなる。FIG. 1 shows a CDQ according to the present invention. A cooling tower 1 for holding red hot coke 2; a blower 5 for sending an inert gas for cooling to the cooling tower 1; a boiler 8 for recovering sensible heat from waste gas of the cooling tower 1; Cyclone 10 that removes waste gas that has passed through 8
A circulation path for returning the waste gas that has passed through the cyclone 10 to the cooling tower 1, a radiation pipe 11 branched from the circulation path for extracting a part of the waste gas as surplus gas 32, and a branch from the radiation pipe 11, And a bag filter 13 for collecting excess gas 32 collected as combustible gas.
【００１１】本発明のポイントは、上記バッグ・フィル
タ１３の下部にダスト２５を連続的に抜き出す排出手段
２３を設け、上記ボイラ８とサイクロン１０との間を結
ぶ配管９に、前記排出手段２３からの微細粒ダスト２５
の搬送管２４を接続したことにある。つまり、バッグ・
フィルタ１３で捕集した微細粒のダスト２５を、該排出
手段２３から、連続的に抜き出し、上記ボイラ８とサイ
クロン１０との間を結ぶ既設の配管９に落とし、既設の
サイクロン１０に捕集させるのである。その際、バッグ
・フィルタ１３からは、余剰ガス３２の一部が、微細粒
ダスト２５と共に、該排出手段２３を通り、サイクロン
１０へ流れるようになる。勿論、図１で明らかなよう
に、既設ボイラ８からの前記低温排出不活性ガス３１
が、上記排出手段２３を逆流する恐れもある。その逆流
を防止するため、本発明に係るＣＤＱは、上記ブロア５
と各所に配置したガス流量の調整弁２９を適切に操作し
て、運転されるのである。このように余剰ガス３２の一
部を、前記循環路に流れるようにしたので、放散管１１
を経て余剰ガス３２流路に導くガスの増量が可能となっ
た。ガスの増量は、その熱容量を増すので、ガス温度の
降下を遅らせる結果になる。本発明では、その増量を前
記希釈用空気の増加で行うようにしたのである。The point of the present invention is that a discharge means 23 for continuously extracting dust 25 is provided below the bag filter 13 and the pipe 9 connecting the boiler 8 and the cyclone 10 is connected to the discharge means 23. Fine dust 25
Is connected. In other words, bags
The fine dust 25 collected by the filter 13 is continuously extracted from the discharge means 23, dropped into the existing pipe 9 connecting the boiler 8 and the cyclone 10, and collected by the existing cyclone 10. It is. At this time, a part of the surplus gas 32 flows from the bag filter 13 together with the fine dust 25 to the cyclone 10 through the discharge means 23. Of course, as apparent from FIG. 1, the low-temperature discharge inert gas 31 from the existing boiler 8 is used.
However, there is a risk that the discharge means 23 flows backward. In order to prevent the backflow, the CDQ according to the present invention uses the blower 5
Thus, the operation is performed by appropriately operating the gas flow rate adjusting valve 29 disposed in each place. As described above, a part of the surplus gas 32 is caused to flow to the circulation path,
Thus, the amount of gas guided to the surplus gas 32 flow path can be increased. Increasing the gas will increase its heat capacity, resulting in a slower drop in gas temperature. In the present invention, the increase is carried out by increasing the dilution air.
【００１２】なお、図１では、上記排出手段に、スパイ
ラル・コンベア２３を用いているが、本発明はそれに限
るものではなく、気体搬送等、連続排出が可能であれば
いかなる手段でも良い。本発明に係るＣＤＱを、余剰ガ
スの回収量が４０００Ｎｍ3 ／時間になるような条件で
運転した。その際、バッグ・フィルタ１３の通過ガス量
を従来より約２０ｖｏｌ％増加させた。その結果、バッ
グ・フィルタ１３の入口部で通過ガスの温度は、まだ約
１９０℃を維持していた。また、スパイラル・コンベア
２３出口でのガス温度は、約１４０℃であり、従来のよ
うなドレン化に伴うトラブルは、一切解消された。In FIG. 1, the spiral conveyor 23 is used as the discharging means. However, the present invention is not limited to this, and any means such as gas conveyance can be used as long as continuous discharging is possible. The CDQ according to the present invention was operated under conditions such that the amount of surplus gas recovered was 4000 Nm 3 / hour. At that time, the amount of gas passing through the bag / filter 13 was increased by about 20 vol% as compared with the conventional case. As a result, the temperature of the passing gas at the inlet of the bag filter 13 was still maintained at about 190 ° C. Further, the gas temperature at the outlet of the spiral conveyor 23 was about 140 ° C., and any troubles associated with the conventional drainage were eliminated.
【００１３】[0013]
【発明の効果】以上述べたように、本発明により、既存
のＣＤＱに小規模な改善を施すだけで、バッグ・フィル
タのダスト排出系内でのドレンによる閉塞が防止され、
円滑な操業と該設備の寿命延長が可能となった。その結
果、余剰ガスを可燃性ガスとして、経済的に回収できる
ようになった。As described above, according to the present invention, the clogging of the bag / filter with the drain in the dust discharge system can be prevented by making a small-scale improvement to the existing CDQ.
Smooth operation and extension of the service life of the equipment became possible. As a result, surplus gas can be economically recovered as combustible gas.
【図１】本発明に係るＣＤＱを示す図である。FIG. 1 is a diagram showing a CDQ according to the present invention.
【図２】特公平５−５４８７９号公報記載の余剰ガスの
回収方法で使用した装置を示す図である。FIG. 2 is a diagram showing an apparatus used in a method for recovering surplus gas described in Japanese Patent Publication No. 5-54879.
【図３】従来からあるＣＤＱを示す図である。FIG. 3 is a diagram showing a conventional CDQ.
１ 冷却塔 ２ 赤熱コークス ３ コークス（冷コークス） ４ （循環）不活性ガス ５ ブロア ６ 除塵器 ７ 循環路（配管） ８ ボイラ（排熱回収ボイラ） ９ 配管 １０ 除塵器（サイクロン） １１ 放散管 １２ 配管 １３ バッグ・フィルタ １４ 余剰ガス回収用配管 １５ ガス本管 １６ 排出系配管 １７ 排出ブロア １８ ダスト・ビン １９ 加熱器 ２０ Ｎ2 ガス用管 ２１ 吸引ブロア ２２ スチーム・トレース ２３ 排出手段（スパイラル・コンベア） ２４ ダスト搬送管 ２５ 微細粒のダスト ２６ モータ ２７ 希釈空気用ブロア ２８ 空気配管 ２９ 調整弁 ３０ 高温排出不活性ガス ３１ 低温排出不活性ガス ３２ 余剰ガス ３３ ダスト払い落とし用気体（窒素ガス）DESCRIPTION OF SYMBOLS 1 Cooling tower 2 Red hot coke 3 Coke (cold coke) 4 (Circulation) inert gas 5 Blower 6 Dust remover 7 Circulation line (Pipe) 8 Boiler (Exhaust heat recovery boiler) 9 Pipe 10 Dust remover (Cyclone) 11 Dispersion pipe 12 piping 13 bag filter 14 excess gas collection piping 15 gas mains 16 discharge piping 17 discharge blower 18 dust bin 19 heater 20 N 2 gas pipe 21 the suction blower 22 steam tracing 23 discharge means (spiral conveyor) Reference Signs List 24 Dust transfer pipe 25 Fine-grain dust 26 Motor 27 Blower for dilution air 28 Air pipe 29 Regulator valve 30 High-temperature discharge inert gas 31 Low-temperature discharge inert gas 32 Excess gas 33 Dust removal gas (nitrogen gas)
Claims (2)
却塔に冷却用の不活性ガスを送るブロアと、該冷却塔の
廃ガスからその顕熱を回収するボイラと、該ボイラを通
過した廃ガスの除塵を行う除塵器と、該除塵器を経た廃
ガスを前記冷却塔へ戻す循環路と、該循環路の上記ブロ
アから冷却塔までの間で分岐され可燃ガスとして回収さ
れる余剰ガスを集塵するバッグ・フィルタとからなるコ
ークス乾式消火設備において、 上記バッグ・フィルタの下部にダストを連続的に抜き出
す排出手段を設け、上記ボイラと除塵器との間を結ぶ配
管に、前記排出手段からのダスト搬送管を接続したこと
を特徴とするコークス乾式消火設備。1. A cooling tower for holding red hot coke, a blower for sending an inert gas for cooling to the cooling tower, a boiler for recovering sensible heat from waste gas of the cooling tower, and a boiler passing through the boiler A dust remover for removing dust from the waste gas, a circulation path for returning the waste gas passing through the dust remover to the cooling tower, and a surplus gas branched from the blower of the circulation path to the cooling tower and collected as combustible gas A coke dry fire extinguishing system comprising a bag and a filter for collecting dust, wherein a discharge means for continuously extracting dust is provided below the bag and filter, and a pipe connecting the boiler and the dust remover is provided with the discharge means. Dry fire extinguishing equipment characterized by connecting a dust transfer pipe from Japan.
したことを特徴とする請求項１記載のコークス乾式消火
設備。2. The coke dry fire extinguishing system according to claim 1, wherein said discharging means is a spiral conveyor.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP18939296A JP3514044B2 (en) | 1996-07-18 | 1996-07-18 | Coke dry fire extinguishing equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP18939296A JP3514044B2 (en) | 1996-07-18 | 1996-07-18 | Coke dry fire extinguishing equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH1036850A true JPH1036850A (en) | 1998-02-10 |
| JP3514044B2 JP3514044B2 (en) | 2004-03-31 |
Family
ID=16240546
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP18939296A Expired - Fee Related JP3514044B2 (en) | 1996-07-18 | 1996-07-18 | Coke dry fire extinguishing equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3514044B2 (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101143169B1 (en) | 2010-09-13 | 2012-05-08 | 주식회사 포스코 | Apparatus for discharging coke powder |
| CN102786950A (en) * | 2012-08-06 | 2012-11-21 | 山西鑫立能源科技有限公司 | Dry quenching exhaust gas generation and combustion heating method |
| KR101282328B1 (en) * | 2010-12-03 | 2013-07-17 | 주식회사 후상 | dust collecting apparatus of cokes oven pusher car |
| KR101434646B1 (en) * | 2013-02-06 | 2014-08-26 | 주식회사 후상 | Wind shield device of the coke oven |
-
1996
- 1996-07-18 JP JP18939296A patent/JP3514044B2/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101143169B1 (en) | 2010-09-13 | 2012-05-08 | 주식회사 포스코 | Apparatus for discharging coke powder |
| KR101282328B1 (en) * | 2010-12-03 | 2013-07-17 | 주식회사 후상 | dust collecting apparatus of cokes oven pusher car |
| CN102786950A (en) * | 2012-08-06 | 2012-11-21 | 山西鑫立能源科技有限公司 | Dry quenching exhaust gas generation and combustion heating method |
| KR101434646B1 (en) * | 2013-02-06 | 2014-08-26 | 주식회사 후상 | Wind shield device of the coke oven |
Also Published As
| Publication number | Publication date |
|---|---|
| JP3514044B2 (en) | 2004-03-31 |
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