JP6270610B2 - Coke oven furnace combustion gas supply device - Google Patents
Coke oven furnace combustion gas supply device Download PDFInfo
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- JP6270610B2 JP6270610B2 JP2014089304A JP2014089304A JP6270610B2 JP 6270610 B2 JP6270610 B2 JP 6270610B2 JP 2014089304 A JP2014089304 A JP 2014089304A JP 2014089304 A JP2014089304 A JP 2014089304A JP 6270610 B2 JP6270610 B2 JP 6270610B2
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- 239000000571 coke Substances 0.000 title claims description 46
- 239000000567 combustion gas Substances 0.000 title claims description 36
- 238000003763 carbonization Methods 0.000 claims description 36
- 239000007789 gas Substances 0.000 claims description 22
- 238000004939 coking Methods 0.000 claims description 8
- 238000000197 pyrolysis Methods 0.000 description 13
- 239000003245 coal Substances 0.000 description 10
- 238000002485 combustion reaction Methods 0.000 description 9
- 238000000034 method Methods 0.000 description 8
- 230000007246 mechanism Effects 0.000 description 5
- 238000012423 maintenance Methods 0.000 description 3
- 230000006835 compression Effects 0.000 description 2
- 238000007906 compression Methods 0.000 description 2
- 238000001125 extrusion Methods 0.000 description 2
- 238000005338 heat storage Methods 0.000 description 2
- 230000001174 ascending effect Effects 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 238000010000 carbonizing Methods 0.000 description 1
- 230000009194 climbing Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000003111 delayed effect Effects 0.000 description 1
- 238000003795 desorption Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000017525 heat dissipation Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
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- Coke Industry (AREA)
Description
本発明は、コークス炉の各炭化室の両側開口部に設置した炉蓋に形成され、炭化室と連通するガス通路に、燃焼用ガスを供給するコークス炉炉蓋の燃焼用ガス供給装置に関する。 The present invention relates to a combustion gas supply apparatus for a coke oven furnace lid, which is formed in a furnace lid installed at both side openings of each carbonization chamber of a coke oven and supplies combustion gas to a gas passage communicating with the carbonization chamber.
通常、コークス炉は、炉体の下部に蓄熱室が配置されると共に、その上部に燃焼室と炭化室とが交互に配列されてなり、炭化室の上部に設けた装入口から石炭を装入し、燃焼室からの伝熱により炭化室内(炉内)で石炭を乾留しコークスを製造する。炭化室内に装入された石炭の乾留が終了すると、各炭化室の両側の開口部に設置した炉蓋を開放する。次いで、一側の開口部側に配置された押出機によって炭化室内のコークスを他側の開口部から排出し、ガイド車を介してコークス乾式消火設備(CDQ)用のバケットあるいは消火車に回収する。 Normally, a coke oven has a heat storage chamber at the lower part of the furnace body, and combustion chambers and carbonization chambers are alternately arranged at the upper part, and coal is charged from an inlet provided at the upper part of the carbonization chamber. The coal is then carbonized in the carbonization chamber (furnace) by heat transfer from the combustion chamber to produce coke. When the carbonization of the coal charged in the carbonization chamber is completed, the furnace lids installed at the openings on both sides of each carbonization chamber are opened. Next, the coke in the carbonization chamber is discharged from the opening on the other side by an extruder disposed on the opening on one side, and is collected into a bucket for a coke dry fire extinguishing equipment (CDQ) or a fire extinguisher via a guide wheel. .
このようにコークス炉においては、コークスの排出の都度、炉蓋が開放され、また、乾留中も炉蓋は外気に晒されるので、特に炭化室の両側開口部近傍において熱放散が大きくなる。したがって、炭化室の両側開口部近傍では、中央部より乾留(コークス化)が遅れることが避けられない。 Thus, in the coke oven, the furnace lid is opened each time the coke is discharged, and the furnace lid is exposed to the outside air even during dry distillation, so that heat dissipation is increased particularly in the vicinity of both side openings of the carbonization chamber. Therefore, in the vicinity of the opening on both sides of the carbonization chamber, it is inevitable that dry distillation (coking) is delayed from the center.
その対策の一つとして、炉蓋に加熱機能を持たせるため、炉蓋に形成したガス通路に燃焼用ガス(空気又は酸素)を吹き込む技術が知られている。例えば特許文献1には、コークス炉で石炭を乾留する際に発生するコークス炉ガスを炉蓋に形成したガス通路へ導入し、乾留中に燃焼用ガスを吹き込んでコースク炉ガスを燃焼させ、炭化室の両側開口部(窯口部)の石炭の乾留を促進する方法において、燃焼用ガスをコークス炉の炉頂より炉蓋に導き、炉高方向の任意の複数位置からガス通路へ吹き込む技術が開示されている。 As one of countermeasures, a technique is known in which combustion gas (air or oxygen) is blown into a gas passage formed in the furnace lid in order to give the furnace lid a heating function. For example, in Patent Document 1, coke oven gas generated when carbonizing coal in a coke oven is introduced into a gas passage formed in the furnace lid, combustion gas is blown during carbonization to burn the coke oven gas, and carbonization is performed. In the method of promoting the dry distillation of coal at both side openings (kiln opening) of the chamber, there is a technique in which the combustion gas is guided from the top of the coke oven to the furnace lid and blown into the gas passage from any plural positions in the furnace height direction. It is disclosed.
しかし、特許文献1の技術では炉蓋外から炉蓋に燃焼用ガスを導く必要があり、そのためのガス配管は、炭化室からコークスを排出するために炉蓋を開放及び閉止する度毎に炉蓋と脱着する必要がある。例えば、炭化室が100室あり各炭化室から20時間毎にコークスを排出する場合、平均して12分間毎に脱着が必要である。特許文献1の技術ではガス配管の脱着にワンタッチ脱着機構を採用しているものの、その脱着には作業者の操作が必要であり、その労力は多大である。 However, in the technique of Patent Document 1, it is necessary to introduce combustion gas from the outside of the furnace lid to the furnace lid, and the gas pipe for that purpose is provided every time the furnace lid is opened and closed in order to discharge coke from the carbonization chamber. It is necessary to remove the lid. For example, when there are 100 carbonization chambers and coke is discharged from each carbonization chamber every 20 hours, desorption is required on average every 12 minutes. Although the technique of Patent Document 1 employs a one-touch detachment mechanism for detaching a gas pipe, an operator operation is required for the detachment, and the labor is great.
一方、特許文献2には、空気吸引パイプに圧縮コイルバネを介して閉塞弁盤を設け、この閉塞弁盤を炉内圧の変化に対応して自己制御動作で開閉する技術が開示されている。しかし、特許文献2の技術を実施するには、炉内圧が−1〜−15mmAqという微小圧力下で制御を行う必要があるため、圧縮コイルバネは通常のバネ設計ができず、制御動作の安定性に問題があると共に、メンテナンスにも労力を要する。 On the other hand, Patent Document 2 discloses a technique in which a closed valve disc is provided on an air suction pipe via a compression coil spring, and this closed valve disc is opened and closed by a self-control operation in response to a change in furnace pressure. However, in order to implement the technique of Patent Document 2, it is necessary to perform control under a very small pressure of −1 to −15 mmAq in the furnace, and therefore, the compression coil spring cannot be designed normally, and the stability of the control operation is not possible. In addition to problems, maintenance also requires effort.
本発明が解決しようとする課題は、コークス炉の各炭化室の両側開口部に設置した炉蓋に形成したガス通路に燃焼用ガスを供給するにあたって、多大な労力をかけることなく、かつメンテナンスを頻繁に行う必要もなく、簡単な構成で燃焼用ガスを供給することができる技術を提供することにある。 The problem to be solved by the present invention is to supply the combustion gas to the gas passage formed in the furnace lid installed in the opening on both sides of each coking chamber of the coke oven without much effort and maintenance. An object of the present invention is to provide a technique capable of supplying a combustion gas with a simple configuration without requiring frequent operations.
上記課題を解決するにあたり、本発明者らが炭化室への燃焼用空気の供給の必要性について研究した結果、燃焼用空気を供給する時期は、炉内圧が負圧になる乾留の中期ないし末期だけで十分であることがわかった。このことから本発明者らは、燃焼用ガスを供給するための燃焼用ガス供給路に開閉弁を設け、炉内圧が正圧になる乾留の初期は開閉弁を閉め、炉内圧が負圧になる乾留の中期ないし末期に開閉弁を開けるようにすれば、簡単な構成で必要十分な燃焼用空気の供給が可能になるという発想を得、更に、開閉弁を開閉する弁開閉手段をコークス炉の移動機械に設けることに想到し、本発明を完成させるに至った。 In solving the above problems, the present inventors have studied the necessity of supplying combustion air to the carbonization chamber, and as a result, the period of supplying combustion air is from the middle to the end of dry distillation where the furnace pressure is negative. It turns out that just enough. From this, the present inventors provided an on-off valve in the combustion gas supply passage for supplying combustion gas, closed the on-off valve at the initial stage of dry distillation when the furnace pressure becomes positive, and the furnace pressure became negative. The idea is that if the on-off valve is opened during the middle or final stage of dry distillation, it will be possible to supply necessary and sufficient combustion air with a simple structure. The present invention has been completed by conceiving that it is provided in a mobile machine.
すなわち本発明によれば、コークス炉の各炭化室の両側開口部に設置した炉蓋に形成され、炭化室と連通するガス通路に、燃焼用ガスを供給するコークス炉炉蓋の燃焼用ガス供給装置であって、各炉蓋に、燃焼用ガスを前記ガス通路に供給するための燃焼用ガス供給路を設けると共に、前記燃焼用ガス供給路に開閉弁を設け、コークス炉の移動機械に、前記開閉弁を開閉する弁開閉手段を設けてなる、コークス炉炉蓋の燃焼用ガス供給装置が提供される。 That is, according to the present invention, the combustion gas supply for the coke oven furnace lid is formed in the furnace lids installed at both side openings of each coking chamber of the coke oven and supplies the combustion gas to the gas passage communicating with the carbonization chamber. A combustion gas supply path for supplying combustion gas to the gas passage is provided in each furnace lid, and an open / close valve is provided in the combustion gas supply path. There is provided a coke oven furnace combustion gas supply device provided with valve opening / closing means for opening and closing the opening / closing valve.
本発明において、前記弁開閉手段は、前記開閉弁を開にする開手段と、前記開閉弁を閉にする閉手段と個別に備えたものとすることができる。 In the present invention, the valve opening / closing means may include an opening means for opening the opening / closing valve and a closing means for closing the opening / closing valve.
本発明によれば、炉蓋側に開閉弁を設け、移動機械側に弁開閉手段を設けるという簡単な構成で、必要十分な燃焼用空気の供給が可能になる。すなわち、コークス炉の各炭化室の両側開口部に設置した炉蓋に形成したガス通路に燃焼用ガスを供給するにあたって、多大な労力をかけることなく、かつメンテナンスを頻繁に行う必要もなく、簡単な構成で燃焼用ガスを供給することができる。また、弁開閉手段をコークス炉に付帯する移動機械(押出機及びガイド車)に設置することで、多大な費用をかけることなく設置できる。 According to the present invention, it is possible to supply necessary and sufficient combustion air with a simple configuration in which an opening / closing valve is provided on the furnace lid side and a valve opening / closing means is provided on the mobile machine side. That is, when supplying combustion gas to the gas passages formed in the furnace lids installed at the openings on both sides of each coking chamber of the coke oven, no effort is required and maintenance is not required frequently. Combustion gas can be supplied with a simple configuration. Further, by installing the valve opening / closing means in a moving machine (extruder and guide car) attached to the coke oven, it can be installed without much cost.
以下、図面に示す実施例に基づき本発明の実施の形態を説明する。 Embodiments of the present invention will be described below based on examples shown in the drawings.
図1は、本発明の一実施例による燃焼用ガス供給装置の構成を概念的に示す平面図、図2は、図1の燃焼用ガス供給装置を適用したコークス炉の炭化室及びコークス炉炉蓋の構成を示し、(a)はその概略縦断面図、(b)は開閉弁の正面図である。 FIG. 1 is a plan view conceptually showing the structure of a combustion gas supply device according to one embodiment of the present invention. FIG. 2 is a coking chamber and coke oven furnace of a coke oven to which the combustion gas supply device of FIG. 1 is applied. The structure of a lid | cover is shown, (a) is the schematic longitudinal cross-sectional view, (b) is a front view of an on-off valve.
先に説明したとおりコークス炉は、炉体の下部に蓄熱室が配置されると共に、その上部に燃焼室と炭化室とが交互に配列されてなる。図1では燃焼室を省略して示しており、複数(実施例では100室)の炭化室10が炉団長方向に配列され、各炭化室10の両側開口部には炉蓋20が設置されている。また、これらの炭化室10の両側には、コークス炉の移動機械である押出機30及びガイド車40が炉団長方向に移動可能に配置されている。押出機30及びガイド車40は周知のとおり、押出機30の押出ラム31による炭化室10からのコークスの排出動作に合わせて相互に同調して移動する。なお、図示は省略しているが、コークスが排出された炭化室に再度石炭を装入する装入車(装炭車)も、押出機30及びガイド車40と同調して移動する。 As described above, the coke oven has a heat storage chamber disposed in the lower portion of the furnace body, and combustion chambers and carbonization chambers are alternately arranged in the upper portion thereof. In FIG. 1, combustion chambers are omitted, and a plurality (100 in the embodiment) of carbonization chambers 10 are arranged in the length direction of the furnace group, and furnace lids 20 are installed at both side openings of the carbonization chambers 10. Yes. In addition, on both sides of the carbonization chamber 10, an extruder 30 and a guide wheel 40, which are coke oven moving machines, are arranged so as to be movable in the length direction of the furnace group. As is well known, the extruder 30 and the guide wheel 40 move in synchronization with each other in accordance with the discharge operation of the coke from the carbonization chamber 10 by the extrusion ram 31 of the extruder 30. In addition, although illustration is abbreviate | omitted, the charging vehicle (charged car) which charges coal in the carbonization chamber where coke was discharged again moves in synchronization with the extruder 30 and the guide wheel 40.
図2(a)に示すように、各炭化室10の両側開口部に設置される炉蓋20の内側(炭化室10側)には、炭化室10に連通するガス通路21が炉高方向に伸びるように形成されている。そして、各炉蓋20には、そのガス通路21に燃焼用ガス(外気)を供給するための燃焼用ガス供給路50が設けられている。実施例では、炉高方向の2箇所に燃焼用ガス供給路50が設けられ、各燃焼用ガス供給路50の炉外側の端部に開閉弁60が設けられている。開閉弁60は例えばボールバルブとすることができ、図2(b)に示すように、弁アーム61が実線の位置にあるときは閉となり、破線の位置まで回転させると開となる。 As shown in FIG. 2A, a gas passage 21 communicating with the carbonization chamber 10 is provided in the furnace height direction on the inner side (carbonization chamber 10 side) of the furnace lid 20 installed at both side openings of each carbonization chamber 10. It is formed to stretch. Each furnace lid 20 is provided with a combustion gas supply passage 50 for supplying combustion gas (outside air) to the gas passage 21 thereof. In the embodiment, combustion gas supply passages 50 are provided at two locations in the furnace height direction, and on-off valves 60 are provided at the outer ends of the combustion gas supply passages 50. The on-off valve 60 can be a ball valve, for example, and is closed when the valve arm 61 is at the solid line position and opened when rotated to the broken line position, as shown in FIG.
一方、図1に示すように、押出機30及びガイド車40には、開閉弁60を開閉するための弁開閉手段70が設けられている。実施例において弁開閉手段60は、開閉弁60を開にする開手段71と、開閉弁60を閉にする閉手段72とを個別に備えている。 On the other hand, as shown in FIG. 1, the extruder 30 and the guide wheel 40 are provided with valve opening / closing means 70 for opening and closing the opening / closing valve 60. In the embodiment, the valve opening / closing means 60 individually includes an opening means 71 for opening the opening / closing valve 60 and a closing means 72 for closing the opening / closing valve 60.
図3は、開手段71の構成の一例を概念的に示す説明図である。開手段71は、第1エアシリンダ71a、第2エアシリンダ71b及び弁開閉アーム71cを備えている。第2エアシリンダ71bは、第1エアシリンダ71aのシリンダロッドの先端に装着されており、第1エアシリンダ71aの駆動により進退する。また、弁開閉アーム71cは第2エアシリンダ71bに装着されており、第2エアシリンダ71bの駆動により上下方向に回転する。 FIG. 3 is an explanatory diagram conceptually showing an example of the configuration of the opening means 71. The opening means 71 includes a first air cylinder 71a, a second air cylinder 71b, and a valve opening / closing arm 71c. The second air cylinder 71b is attached to the tip of the cylinder rod of the first air cylinder 71a, and moves forward and backward by driving the first air cylinder 71a. The valve opening / closing arm 71c is mounted on the second air cylinder 71b, and rotates in the vertical direction by driving the second air cylinder 71b.
開手段71による開閉弁60の開操作は、次のとおりである。まず、図3(a)の初期位置から第1エアシリンダ71aを駆動させて第2エアシリンダ71b及び弁開閉アーム71cを前進させ、弁開閉アーム71cの先端を開閉弁60の弁アーム61に引っ掛ける。その状態で、第2エアシリンダ71bを駆動させて、図3(b)に示すように弁開閉アーム71cを上方に回転させる。これにより、開閉弁60が開となる。その後、第1エアシリンダ71a及び第2エアシリンダ71bを駆動させて図3(a)の初期位置に戻す。 The opening operation of the on-off valve 60 by the opening means 71 is as follows. First, the first air cylinder 71a is driven from the initial position of FIG. 3A to advance the second air cylinder 71b and the valve opening / closing arm 71c, and the tip of the valve opening / closing arm 71c is hooked on the valve arm 61 of the opening / closing valve 60. . In this state, the second air cylinder 71b is driven to rotate the valve opening / closing arm 71c upward as shown in FIG. Thereby, the on-off valve 60 is opened. Thereafter, the first air cylinder 71a and the second air cylinder 71b are driven to return to the initial positions in FIG.
一方、閉手段72については詳細な説明は省略するが、図3に示した開手段71と同様の構成により、開閉弁60を閉にできることは当業者に自明である。なお、これらの開手段71及び閉手段72の駆動源となる圧縮空気は、図1に示す駆動源73から供給される。 On the other hand, although detailed description of the closing means 72 is omitted, it is obvious to those skilled in the art that the on-off valve 60 can be closed by the same configuration as the opening means 71 shown in FIG. In addition, the compressed air which becomes a drive source of these opening means 71 and the closing means 72 is supplied from the drive source 73 shown in FIG.
次に、本実施例の燃焼用ガス供給装置の動作を説明する。 Next, the operation of the combustion gas supply apparatus of this embodiment will be described.
図4は、コークス炉の炭化室において、石炭の装入からコークスの排出まで間(実施例では20時間)の炭化室の内圧(炉内圧)の変化を概念的に示す。同図に示すように、乾留の初期はガス発生量が多く炉内圧は正圧となるが、炉内ガスはコークス炉の上昇管11(図2参照)から炉外に強制的に排出され、乾留の中期ないし末期ではガス発生量が減少するため、乾留の中期ないし末期になると炉内圧は負圧になる。 FIG. 4 conceptually shows changes in the internal pressure (furnace pressure) of the coking chamber in the coking chamber of the coke oven from the charging of the coal to the discharging of the coke (20 hours in the example). As shown in the figure, at the initial stage of dry distillation, the amount of gas generated is large and the pressure inside the furnace becomes positive, but the gas inside the furnace is forcibly discharged out of the furnace from the ascending pipe 11 of the coke oven (see FIG. 2), Since the amount of gas generation decreases in the middle or end of dry distillation, the furnace pressure becomes negative in the middle or end of dry distillation.
本発明では、この炉内圧が負圧になる乾留の中期ないし末期に開閉弁60を開けることで、負圧を利用して燃焼用ガス(外気)を炭化室10に供給する。そして、乾留が終わってコークス排出後、次の石炭が装入される前に開閉弁60を閉める。これにより、炉内圧が正圧になる乾留の初期に炉内ガスが吹き出すことを防止する。これらの開閉弁60の開閉のタイミングは、コークス炉の操業パターンに合せて適宜設定すればよい。要するに、各炭化室について、乾留の中期ないし末期に開閉弁60を開け、次の石炭が装入される前に開閉弁60を閉めるというサイクルを維持できればよく、そのサイクルを維持できるようコークス炉の移動機械(押出機30及びガイド車40)の移動パターンを設定すればよい。 In the present invention, the gas for combustion (outside air) is supplied to the carbonization chamber 10 by utilizing the negative pressure by opening the on-off valve 60 in the middle or end of the dry distillation where the pressure in the furnace is negative. Then, after the dry distillation is finished and the coke is discharged, the on-off valve 60 is closed before the next coal is charged. This prevents the in-furnace gas from being blown out at the initial stage of dry distillation when the in-furnace pressure becomes positive. The opening / closing timing of these on-off valves 60 may be set as appropriate according to the operation pattern of the coke oven. In short, for each carbonization chamber, it is only necessary to maintain a cycle in which the on-off valve 60 is opened in the middle or end of dry distillation and the on-off valve 60 is closed before the next coal is charged. What is necessary is just to set the movement pattern of a moving machine (the extruder 30 and the guide wheel 40).
なお、前記実施例では本発明の弁開閉手段をコークス炉の移動機械として元々ある押出機30及びガイド車40に設けたが、他の適用例として、コークス炉の移動機械として、押出機、ガイド車に同調して移動する移動台車を各々設け、これらの移動台車に弁開閉機構を設けてもよい。この移動台車も本発明でいう「コークス炉の移動機械」である。 In the above embodiment, the valve opening / closing means of the present invention is provided in the original extruder 30 and guide wheel 40 as a coke oven moving machine. However, as another application example, the coke oven moving machine includes an extruder and a guide. It is also possible to provide each moving carriage that moves in synchronization with the vehicle, and to provide a valve opening / closing mechanism for these moving carriages. This moving carriage is also a “coke oven moving machine” in the present invention.
また、実施例では、弁開閉手段70として、開閉弁60を開にする開手段71と、開閉弁60を閉にする閉手段72とを個別に設け、これらの開手段71及び閉手段72によって、炉長方向に並列する炭化室10の開閉弁60を同じタイミングで開閉するようにしたが、開手段71及び閉手段72を統合して一つの弁開閉手段70とし、この弁開閉手段を炉長方向に移動可能として、各炭化室10の開閉弁60を開閉するようにすることもできる。また、実施例では、開手段71及び閉手段72としてエアシリンダを利用した機構を使用したが、開閉弁60を開閉する機構としては、その他様々な機構が使用できることは、当業者に自明である。 Further, in the embodiment, as the valve opening / closing means 70, an opening means 71 for opening the opening / closing valve 60 and a closing means 72 for closing the opening / closing valve 60 are provided separately, and by these opening means 71 and closing means 72, The open / close valve 60 of the carbonization chamber 10 arranged in parallel in the furnace length direction is opened and closed at the same timing. However, the opening means 71 and the closing means 72 are integrated into a single valve opening / closing means 70, and this valve opening / closing means is used as a furnace. The on-off valve 60 of each carbonization chamber 10 can be opened and closed so as to be movable in the long direction. In the embodiment, a mechanism using an air cylinder is used as the opening means 71 and the closing means 72. However, it is obvious to those skilled in the art that various other mechanisms can be used as the mechanism for opening and closing the on-off valve 60. .
10 炭化室
11 上昇管
20 炉蓋
21 ガス通路
30 押出機(コークス炉の移動機械)
31 押出ラム
40 ガイド車(コークス炉の移動機械)
50 燃焼用ガス供給路
60 開閉弁
61 弁アーム
70 弁開閉手段
71 開手段
71a 第1エアシリンダ
71b 第2エアシリンダ
71c 弁開閉アーム
DESCRIPTION OF SYMBOLS 10 Carbonization chamber 11 Climbing pipe 20 Furnace lid 21 Gas passage 30 Extruder (moving machine of coke oven)
31 Extrusion ram 40 Guide car (coke oven moving machine)
50 Combustion gas supply path 60 Opening / closing valve 61 Valve arm 70 Valve opening / closing means 71 Opening means 71a First air cylinder 71b Second air cylinder 71c Valve opening / closing arm
Claims (2)
各炉蓋に、燃焼用ガスを前記ガス通路に供給するための燃焼用ガス供給路を設けると共に、前記燃焼用ガス供給路に開閉弁を設け、
コークス炉の移動機械に、前記開閉弁を開閉する弁開閉手段を設けてなる、コークス炉炉蓋の燃焼用ガス供給装置。 A combustion gas supply device for a coke oven lid that is formed in a furnace lid installed at both side openings of each coking chamber of a coke oven and supplies a combustion gas to a gas passage communicating with the carbonization chamber,
Each furnace lid is provided with a combustion gas supply passage for supplying combustion gas to the gas passage, and an open / close valve is provided in the combustion gas supply passage,
A combustion gas supply device for a coke oven furnace lid, wherein a valve opening and closing means for opening and closing the on-off valve is provided in a coke oven moving machine.
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