JP5192988B2 - Continuous processing equipment for painted steel sheet - Google Patents

Continuous processing equipment for painted steel sheet Download PDF

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JP5192988B2
JP5192988B2 JP2008285820A JP2008285820A JP5192988B2 JP 5192988 B2 JP5192988 B2 JP 5192988B2 JP 2008285820 A JP2008285820 A JP 2008285820A JP 2008285820 A JP2008285820 A JP 2008285820A JP 5192988 B2 JP5192988 B2 JP 5192988B2
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steel plate
radiant tube
steel sheet
continuous processing
processing apparatus
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JP2010111922A (en
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正明 上山
真一郎 田邉
重信 古賀
政文 矢野
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Nippon Steel Corp
Nippon Steel Engineering Co Ltd
Nippon Steel Plant Designing Corp
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Nippon Steel and Sumitomo Metal Corp
NS Plant Designing Corp
Nippon Steel and Sumikin Engineering Co Ltd
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Description

本発明は、塗装鋼板の連続処理装置に関する。 The present invention relates to a continuous processing apparatus for coated steel sheets.

例えば、塗装膜の乾燥と焼付けを行う塗装鋼板の連続処理装置では、塗装膜を乾燥する乾燥炉には、塗布直後の塗装膜に疵を付けることがなく、塗装膜中の溶媒の突沸を防止しながら溶媒を蒸発させる低温度域での温度制御が可能な横型カテナリー式のラジアントチューブ炉を使用し、乾燥炉の後段に設けられ塗装膜を鋼板に焼付ける焼付け炉には、直火式加熱炉を使用することができる。
ここで、予熱炉と予熱炉の後段に設けられた直火式加熱炉とを有する鋼板の連続焼鈍装置において、直火式加熱炉で生成した燃焼排ガスを予熱炉に供給して予熱炉内の鋼板を加熱することで予熱炉の燃料原単位を低減させ予熱炉の熱効率の向上させるために、予熱炉と直火式加熱炉を連続的に配置し、直火式加熱炉の上流側(燃焼排ガスの流れに対しては下流側)と予熱炉の下流側(燃焼排ガスの流れに対しては上流側)との間に直火式加熱炉で生成した燃焼排ガスを予熱炉に供給する排ガス供給用導管を、予熱炉の上流側(燃焼排ガスの流れに対しては下流側)に燃焼排ガスを排出する煙突に連通するガス排出用導管をそれぞれ設け、更に、排ガス供給用導管の途中とガス排出用導管の途中をダンパを備えたバイパス管で接続することが提案されている(例えば、特許文献1参照)。また、直火式加熱炉で発生した燃焼排ガスを速やかに排出してバーナを効率的に作動させるために、予熱炉を直火式加熱炉に直結し、予熱炉の鋼板出口近傍の直火式加熱炉に近い部分(予熱炉の下流側)と直火式加熱炉を燃焼排ガス煙道で接続し、予熱炉の鋼板入口近くに排出口を設けることが提案されている(例えば、特許文献2参照)。
For example, in a continuous processing equipment for coated steel sheets that drys and bakes the coating film, the drying furnace that dries the coating film does not cause wrinkles on the coating film immediately after coating, preventing sudden boiling of the solvent in the coating film A horizontal catenary type radiant tube furnace that can control the temperature in the low temperature range while evaporating the solvent is used. A furnace can be used.
Here, in a continuous annealing apparatus for a steel sheet having a preheating furnace and a direct-fired heating furnace provided at the subsequent stage of the preheating furnace, the combustion exhaust gas generated in the direct-fired heating furnace is supplied to the preheating furnace to In order to reduce the fuel intensity of the preheating furnace and improve the thermal efficiency of the preheating furnace by heating the steel plate, the preheating furnace and the direct heating furnace are continuously arranged, and the upstream side of the direct heating furnace (combustion) Exhaust gas supply that supplies combustion exhaust gas generated in a direct-fired heating furnace between the downstream side of the exhaust gas flow and the downstream side of the preheating furnace (upstream side of the combustion exhaust gas flow) to the preheating furnace A gas exhaust pipe communicating with the chimney for exhausting the exhaust gas is provided on the upstream side of the preheating furnace (on the downstream side with respect to the combustion exhaust gas flow). It is recommended that a bypass pipe with a damper be connected in the middle of the pipe Is (e.g., see Patent Document 1). Also, in order to quickly discharge the combustion exhaust gas generated in the direct-fired heating furnace and operate the burner efficiently, the preheating furnace is directly connected to the direct-heating furnace, and the direct-fired type near the steel plate outlet of the preheating furnace It has been proposed to connect a portion close to the heating furnace (downstream side of the preheating furnace) and a direct-fired heating furnace with a flue gas flue and provide an outlet near the steel plate inlet of the preheating furnace (for example, Patent Document 2). reference).

特開平6−158182号公報JP-A-6-158182 特開平11−12658号公報Japanese Patent Laid-Open No. 11-12658

特許文献1、2の発明は、連続焼鈍設備に対するものであり、塗装鋼板の乾燥及び焼付けに対するものではない。このため、特許文献1、2の発明では、予熱炉入側がシールロールでシールされ、予熱炉入側からの外気の侵入を遮断することができる。しかし、塗装鋼板の連続処理装置の乾燥炉(例えば、ラジアントチューブ炉あるいは熱風吹付炉等)では、塗装後の塗装膜が乾燥する迄は、鋼板(塗装膜)に触れることができない。このため、乾燥炉、例えば、ラジアントチューブ炉の鋼板入口にシールロールを設けて鋼板入口からの外気の侵入を遮断することができず、ラジアントチューブ炉の鋼板入口から外気がラジアントチューブ炉内に侵入しラジアントチューブ炉の熱効率が低下するという問題が発生する。このため、ラジアントチューブ炉の鋼板入口の扉を塗装鋼板の通過に障害が発生しない限界まで閉じることが必要になるが、扉を限界まで閉じておくと、塗装鋼板の搬送用に加えている張力に変動が生じた場合、塗装鋼板が振動し、扉に衝突して塗装膜に疵が付いたり、鋼板が破断するという問題が発生する。また、直下式加熱炉自体に、煙突と連通する連結管を設けた場合、連結管内に設けたダンパを閉じても直下式加熱炉と煙突との連通を完全に遮断することができないため、煙突のドラフト効果により直下式加熱炉及びラジアントチューブ炉内のガスが吸引される。この場合、直下式加熱炉で発生する燃焼排ガス量を、連結管のダンパを閉じた際の煙突のドラフト効果により吸引されるガス量以下に抑えると、ラジアントチューブ炉の鋼板入口を介してラジアントチューブ炉内に外気が吸い込まれることとなる。更に、直下式加熱炉からドラフト効果で排気される燃焼排ガス分については、その熱量を有効利用できず、ラジアントチューブ炉の熱効率が低下するという問題もある。 The inventions of Patent Documents 1 and 2 are for continuous annealing equipment, not for drying and baking of coated steel sheets. For this reason, in the inventions of Patent Documents 1 and 2, the entrance side of the preheating furnace is sealed with the seal roll, so that intrusion of outside air from the entrance side of the preheating furnace can be blocked. However, in a drying furnace (for example, a radiant tube furnace or a hot air blowing furnace) of a continuous processing apparatus for coated steel sheets, the steel sheet (paint film) cannot be touched until the coated film after coating is dried. For this reason, a seal roll is provided at the steel plate inlet of a drying furnace, for example, a radiant tube furnace, so that intrusion of outside air from the steel plate inlet cannot be blocked, and outside air enters the radiant tube furnace from the steel plate inlet of the radiant tube furnace. However, there arises a problem that the thermal efficiency of the radiant tube furnace is lowered. For this reason, it is necessary to close the door at the entrance of the steel plate of the radiant tube furnace to the limit that does not cause obstacles in the passage of the coated steel plate, but if the door is closed to the limit, the tension applied for conveying the coated steel plate When fluctuation occurs, the coated steel plate vibrates and collides with the door, causing a problem that the coating film is wrinkled or the steel plate is broken. In addition, when the direct heating furnace itself is provided with a connecting pipe that communicates with the chimney, the connection between the direct heating furnace and the chimney cannot be completely blocked even if the damper provided in the connecting pipe is closed. Due to the draft effect, the gas in the direct heating furnace and the radiant tube furnace is sucked. In this case, if the amount of combustion exhaust gas generated in the direct heating furnace is kept below the amount of gas sucked by the draft effect of the chimney when the damper of the connecting pipe is closed, the radiant tube is passed through the steel plate inlet of the radiant tube furnace. Outside air will be sucked into the furnace. Furthermore, regarding the combustion exhaust gas exhausted from the direct heating furnace by the draft effect, the amount of heat cannot be effectively used, and there is a problem that the thermal efficiency of the radiant tube furnace is lowered.

本発明はかかる事情に鑑みてなされたもので、ラジアントチューブ炉の鋼板入口からラジアントチューブ炉深部への外気の侵入を抑制してラジアントチューブ炉の熱効率を向上すると共に鋼板への疵の発生を回避することが可能な塗装鋼板の連続処理装置を提供することを目的とする。 The present invention has been made in view of such circumstances, and suppresses the intrusion of outside air from the steel sheet inlet of the radiant tube furnace to the deep part of the radiant tube furnace to improve the thermal efficiency of the radiant tube furnace and avoid the occurrence of soot on the steel sheet. It aims at providing the continuous processing apparatus of the coated steel plate which can do.

前記目的に沿う本発明に係る塗装鋼板の連続処理装置は、塗装された鋼板が供給されて該鋼板の塗装膜を乾燥する横型カテナリー式のラジアントチューブ炉と、該ラジアントチューブ炉の鋼板出口部に直結し、該ラジアントチューブ炉から排出された前記鋼板を受入れて乾燥後の前記塗装膜を該鋼板に焼付ける直火式加熱炉とを備えた塗装鋼板の連続処理装置において、
前記ラジアントチューブ炉の鋼板入口の直上流側に、前記直火式加熱炉で発生した燃焼排ガスを排気する第1の排気手段を設けている。
The continuous processing apparatus of the coated steel sheet according to the present invention that meets the above-described object is provided in a horizontal catenary type radiant tube furnace that is supplied with a coated steel sheet and dries the coated film of the steel sheet, and a steel sheet outlet portion of the radiant tube furnace. In a continuous processing apparatus for a coated steel sheet, comprising a direct-fired heating furnace that is directly connected and receives the steel sheet discharged from the radiant tube furnace and bakes the coated film after drying on the steel sheet.
First exhaust means for exhausting combustion exhaust gas generated in the direct-fired heating furnace is provided immediately upstream of the steel sheet inlet of the radiant tube furnace.

本発明に係る塗装鋼板の連続処理装置において、前記ラジアントチューブ炉の前記鋼板入口の直下流側に、前記第1の排気手段と連通し該鋼板入口から侵入した外気を吸引するダクトを設けることが好ましい。 In the coated steel sheet continuous processing apparatus according to the present invention, a duct that communicates with the first exhaust means and sucks outside air that has entered from the steel sheet inlet is provided immediately downstream of the steel sheet inlet of the radiant tube furnace. preferable.

本発明に係る塗装鋼板の連続処理装置において、前記直火式加熱炉の鋼板出口部に該鋼板出口部に連通し該鋼板出口部内の燃焼排ガスを排気する第2の排気手段を設け、該第2の排気手段と該鋼板出口部との連通部の直上流側の該鋼板出口部の部位に前記鋼板を通過させ該直火式加熱炉内の燃焼排ガスの流出を抑制する仕切りを設けることが好ましい。
また、本発明にかかる塗装鋼板の連続処理装置において、該塗装鋼板の連続処理装置を水溶性の塗装膜の乾燥及び焼付け装置とすることができる。
ここで、前記水溶性の塗装膜は方向性珪素鋼板の絶縁皮膜であってもよい。
In the continuous processing apparatus for a coated steel sheet according to the present invention, a second exhaust means is provided in the steel plate outlet of the direct-fired heating furnace so as to communicate with the steel plate outlet and exhaust the combustion exhaust gas in the steel plate outlet. A partition for suppressing the outflow of combustion exhaust gas in the direct-fired heating furnace by passing the steel plate through a portion of the steel plate outlet portion immediately upstream of the communication portion between the exhaust means of 2 and the steel plate outlet portion; preferable.
Moreover, the continuous processing apparatus of the coated steel plate concerning this invention can use the continuous processing apparatus of this coated steel plate as a drying and baking apparatus of a water-soluble coating film.
Here, the water-soluble coating film may be an insulating film of a directional silicon steel sheet.

本発明に係る塗装鋼板の連続処理装置においては、ラジアントチューブ炉の鋼板入口の直上流側に、直火式加熱炉で発生した燃焼排ガスを排気する第1の排気手段を設けたので、直火式加熱炉で発生した燃焼排ガスを直火式加熱炉自体に連通する煙突を介して排気する場合、あるいは直火式加熱炉で発生した燃焼排ガスをラジアントチューブ炉の鋼板入口より下流側のラジアントチューブ炉の部位と連通する煙突を介して排気する場合に比べて、ラジアントチューブ炉の鋼板入口を通過させて外部に排出させる燃焼排ガス流量を増加できる。このため、従来は、ラジアントチューブ炉の深部に外気が侵入するのを抑制するため鋼板入口の扉を鋼板の通過が可能となる下限開口度まで閉じていたが、本発明では、ラジアントチューブ炉の鋼板入口を通過する燃焼ガス流量が増加した分だけ、扉の開口度を下限開口度より増加ができる。その結果、鋼板搬送のために鋼板に加えている張力に変動が生じて鋼板のカテナリー(パスライン)が変動しても、鋼板が鋼板入口に設けた扉に接触するのを防止できる。 In the coated steel sheet continuous processing apparatus according to the present invention, the first exhaust means for exhausting the combustion exhaust gas generated in the direct heating furnace is provided immediately upstream of the steel sheet inlet of the radiant tube furnace. When exhaust gas generated in a direct heating furnace is exhausted through a chimney communicating with the direct heating furnace itself, or the exhaust gas generated in the direct heating furnace is radiant tube downstream from the steel plate inlet of the radiant tube furnace Compared with the case of exhausting through a chimney communicating with the furnace part, it is possible to increase the flow rate of the combustion exhaust gas that passes through the steel plate inlet of the radiant tube furnace and is discharged to the outside. For this reason, conventionally, in order to suppress the outside air from entering the deep part of the radiant tube furnace, the door of the steel plate was closed to the lower limit opening degree that allows the steel plate to pass through. The opening degree of the door can be increased from the lower limit opening degree by an amount corresponding to an increase in the flow rate of the combustion gas passing through the steel plate inlet. As a result, even if the tension applied to the steel plate for the steel plate conveyance fluctuates and the catenary (pass line) of the steel plate fluctuates, the steel plate can be prevented from contacting the door provided at the steel plate inlet.

ラジアントチューブ炉内を通過して第1の排気手段で排出される燃焼排ガスの流れで鋼板が加熱でき、ラジアントチューブ炉の燃料原単位が低減してラジアントチューブ炉の熱効率が向上することは言うまでもない。
また、直火式加熱炉自体に、煙突と連通する連結管を設けた場合、連結管のダンパを閉じても煙突のドラフト効果により吸引されるガス量以下に直火式加熱炉の燃焼排ガス量を抑えることができない問題があったが、本発明では、直火式加熱炉自体には第1の排気手段と連通する連結管が設けられていないため、この問題は当然発生しない。更に、直火式加熱炉自体から第1の排気手段に連通する連結管への燃焼排ガスの排気がないため、その燃焼排ガスの熱量をラジアンとチューブ炉において有効利用し、ラジアントチューブ炉の熱効率を上げることは言うまでもない。
It goes without saying that the steel plate can be heated by the flow of the combustion exhaust gas that passes through the radiant tube furnace and is discharged by the first exhaust means, the fuel unit of the radiant tube furnace is reduced, and the thermal efficiency of the radiant tube furnace is improved. .
In addition, if the direct-fired heating furnace itself is provided with a connecting pipe that communicates with the chimney, the combustion exhaust gas amount of the direct-fired heating furnace will be less than the amount of gas drawn by the draft effect of the chimney even if the damper of the connecting pipe is closed However, in the present invention, since the direct-fired heating furnace itself is not provided with a connecting pipe communicating with the first exhaust means, this problem does not naturally occur. Further, since there is no exhaust of the combustion exhaust gas from the direct heating furnace itself to the connecting pipe communicating with the first exhaust means, the heat amount of the combustion exhaust gas is effectively used in the radians and the tube furnace, and the thermal efficiency of the radiant tube furnace is improved. Needless to say to raise it.

本発明に係る塗装鋼板の連続処理装置において、ラジアントチューブ炉の鋼板入口の直下流側に、第1の排気手段と連通し鋼板入口から侵入した外気を吸引するダクトを設ける場合、ラジアントチューブ炉の鋼板入口からラジアントチューブ炉内に外気が侵入してもダクトを介して第1の排気手段で排気することができ、ラジアントチューブ炉の深部にまで外気が侵入し難い。 In the continuous processing apparatus for coated steel sheets according to the present invention, when a duct that communicates with the first exhaust means and sucks outside air that has entered from the steel sheet inlet is provided immediately downstream of the steel sheet inlet of the radiant tube furnace, Even if the outside air enters the radiant tube furnace from the steel sheet inlet, it can be exhausted by the first exhaust means through the duct, and the outside air hardly penetrates to the deep part of the radiant tube furnace.

本発明に係る塗装鋼板の連続処理装置において、直火式加熱炉の鋼板出口部に第2の排気手段及び仕切りを設ける場合、直火式加熱炉の後段に燃焼排ガスが流れ出すのを防止できる。 In the continuous processing apparatus for a coated steel sheet according to the present invention, when the second exhaust means and the partition are provided at the steel sheet outlet of the direct heating furnace, it is possible to prevent the combustion exhaust gas from flowing out to the rear stage of the direct heating furnace.

続いて、添付した図面を参照しつつ、本発明を具体化した実施の形態につき説明し、本発明の理解に供する。
ここで、図1は本発明による方向性珪素鋼板の絶縁皮膜の乾燥及び焼付け装置に適用される一実施の形態に係る塗装鋼板の連続処理装置の説明図、図2は同塗装鋼板の連続処理装置の作用の説明図である。
Next, embodiments of the present invention will be described with reference to the accompanying drawings for understanding of the present invention.
Here, FIG. 1 is an explanatory view of a continuous processing apparatus for coated steel sheets according to one embodiment applied to an insulating film drying and baking apparatus for grain-oriented silicon steel sheets according to the present invention, and FIG. 2 is a continuous processing for the coated steel sheets. It is explanatory drawing of an effect | action of an apparatus.

図1に示すように、本発明による方向性珪素鋼板の絶縁皮膜の乾燥及び焼付け装置に適用される一実施の形態に係る塗装鋼板の連続処理装置10は、塗装された鋼板11が供給されて鋼板11の塗装膜を乾燥する横型カテナリー式のラジアントチューブ炉12と、ラジアントチューブ炉12の鋼板出口部13に直結し、ラジアントチューブ炉12から排出された鋼板11を受入れて乾燥後の塗装膜を鋼板11に焼付ける、例えば、横型カテナリー式の直火式加熱炉14とを備え、ラジアントチューブ炉12の鋼板入口15の直上流側に、直火式加熱炉14で発生しラジアントチューブ炉12内に流入した燃焼排ガスを排気する第1の排気手段16を設けている。以下、詳細に説明する。 As shown in FIG. 1, a coated steel sheet 11 is supplied to a coated steel sheet continuous treatment apparatus 10 according to an embodiment applied to an apparatus for drying and baking an insulating film of a grain-oriented silicon steel sheet according to the present invention. A horizontal catenary-type radiant tube furnace 12 for drying the coating film of the steel plate 11 and a steel plate outlet 13 of the radiant tube furnace 12 are directly connected to the steel plate 11 discharged from the radiant tube furnace 12 and dried. The steel plate 11 is baked, for example, has a horizontal catenary direct-fired heating furnace 14, and is generated in the direct-fired heating furnace 14 immediately upstream of the steel plate inlet 15 of the radiant tube furnace 12. A first exhaust means 16 is provided for exhausting the combustion exhaust gas flowing into the exhaust gas. Details will be described below.

ラジアントチューブ炉12は、水平方向に搬送される鋼板11を上下方向から把持して鋼板11に塗装膜を塗布するコーターロール17の下流側に設けられている。そして、ラジアントチューブ炉12は、塗装膜が塗布された鋼板11が通過する鋼板入口15が上流側端部に設けられ、塗装膜が塗布された鋼板11を加熱して塗装膜を乾燥させる図示しないラジアントチューブ及びコーターロール17と平行に配置されコーターロール17と対となって鋼板11を支える支持ロール18とを内部に備えた乾燥処理部19と、乾燥処理部19の後段に連接して設けられ、ラジアントチューブ炉12から排出する塗装膜が塗布された鋼板11のパスラインの高さ位置を決める排出ロール20(支持ロール18と平行に配置されている)を内部に備えた鋼板出口部13とを有している。ここで、鋼板入口15の開口部が形成されている乾燥処理部19の上流側端部には、上流側端部の外側面上をそれぞれ上下方向に摺動して開口部を覆う対となる上、下仕切り部材21、22を有する扉23が設けられている。 The radiant tube furnace 12 is provided on the downstream side of the coater roll 17 that grips the steel plate 11 conveyed in the horizontal direction from above and below and applies a coating film to the steel plate 11. The radiant tube furnace 12 is provided with a steel plate inlet 15 through which the steel plate 11 coated with the coating film passes at the upstream end, and heats the steel plate 11 coated with the coating film to dry the coating film (not shown). A drying processing unit 19 that is disposed in parallel with the radiant tube and the coater roll 17 and includes a support roll 18 that supports the steel plate 11 in a pair with the coater roll 17, and is connected to the subsequent stage of the drying processing unit 19. A steel plate outlet 13 having a discharge roll 20 (disposed in parallel with the support roll 18) for determining the height position of the pass line of the steel plate 11 coated with the coating film discharged from the radiant tube furnace 12, and have. Here, the upstream end of the drying processing unit 19 in which the opening of the steel plate inlet 15 is formed is a pair that slides in the vertical direction on the outer surface of the upstream end to cover the opening. A door 23 having upper and lower partition members 21 and 22 is provided.

第1の排気手段16は、鋼板入口15の直上流側(手前側)の上方に吸引口が設けられてラジアントチューブ炉12内の燃焼排ガスを鋼板入口15を介してラジアントチューブ炉12外に吸引する燃焼排ガス排出ダクト24と、燃焼排ガス排出ダクト24に接続する第1の煙突25とを有している。そして、ラジアントチューブ炉12の乾燥処理部19の天井で鋼板入口15の直下流側の部位には、第1の排気手段16の第1の煙突25と基部が連通し、先部に鋼板入口15からラジアントチューブ炉12内に侵入した外気を吸引する吸引口が形成されたダクト26が設けられている。ここで、燃焼排ガス排出ダクト24内には第1のダンパ27、ダクト26内には第2のダンパ28がそれぞれ設けられ、燃焼排ガス排出ダクト24の吸引口の縁部にはフード29が取付けられている。 The first exhaust means 16 is provided with a suction port above the upstream side (near side) of the steel plate inlet 15 and sucks the combustion exhaust gas in the radiant tube furnace 12 to the outside of the radiant tube furnace 12 through the steel plate inlet 15. And a first chimney 25 connected to the combustion exhaust gas discharge duct 24. The first chimney 25 and the base of the first exhaust means 16 communicate with a portion of the ceiling of the drying processing unit 19 of the radiant tube furnace 12 and immediately downstream of the steel plate inlet 15, and the steel plate inlet 15 is connected to the front. A duct 26 having a suction port for sucking outside air that has entered the radiant tube furnace 12 is provided. Here, a first damper 27 is provided in the flue gas exhaust duct 24, and a second damper 28 is provided in the duct 26, and a hood 29 is attached to the edge of the suction port of the flue gas exhaust duct 24. ing.

直火式加熱炉14は、ラジアントチューブ炉12の鋼板出口部13と接続し、鋼板出口部13から排出され塗装膜の乾燥が終了した鋼板11を受入れる鋼板入口30を上流側端部に備え、乾燥後の塗装膜を加熱して鋼板11に焼付ける図示しないバーナ及び排出ロール20と平行に配置され排出ロール20と対となって鋼板11を支える支持ロール31とを内部に備えた焼付け処理部32と、焼付け処理部32の後段に連接して設けられ、直火式加熱炉14から排出する塗装膜が焼付けされた鋼板11のパスラインの高さ位置を決める排出ロール34(支持ロール31と平行に配置されている)を内部に備えた鋼板出口部35とを有している。 The direct-fired heating furnace 14 is connected to the steel plate outlet portion 13 of the radiant tube furnace 12 and includes a steel plate inlet 30 that receives the steel plate 11 discharged from the steel plate outlet portion 13 and dried of the coating film at the upstream end portion, A baking processing unit that is provided in parallel with a burner (not shown) that heats the dried coating film and burns it onto the steel plate 11 and a discharge roll 20 and that supports the steel plate 11 in pairs with the discharge roll 20. 32 and a discharge roll 34 (support roll 31 and a support roll 31) that is connected to the subsequent stage of the baking processing unit 32 and determines the height position of the pass line of the steel plate 11 on which the coating film discharged from the direct heating furnace 14 is baked. And a steel plate outlet portion 35 provided in the inside thereof.

また、直火式加熱炉14の鋼板出口部35の中間部には、鋼板出口部35に連通し鋼板出口部35内の燃焼排ガスを排気する第2の排気手段36が設けられ、鋼板出口部35の中間部より上流側(第2の排気手段36と鋼板出口部35との連通部の直上流側)の鋼板出口部35の部位には、塗装膜が焼付けられた鋼板11を通過させ直火式加熱炉14内の燃焼排ガスの流出を抑制する上下対となる仕切り壁37、38を備えた仕切り39が設けられている。ここで、第2の排気手段36は、鋼板出口部35の天井の中間部に接続されて鋼板出口部35内の燃焼排ガスを排気する排ガス排出ダクト40と、排ガス排出ダクト40に接続する第2の煙突41とを有している。そして、排ガス排出ダクト40には第3のダンパ42が設けられている。これによって、直火式加熱炉14の後段に燃焼排ガスが流出するのを防止できる。 In addition, a second exhaust means 36 that communicates with the steel plate outlet portion 35 and exhausts the combustion exhaust gas in the steel plate outlet portion 35 is provided at an intermediate portion of the steel plate outlet portion 35 of the direct-fired heating furnace 14. The steel plate 11 on which the coating film is baked is passed through the portion of the steel plate outlet 35 on the upstream side of the intermediate portion 35 (immediately upstream of the communication portion between the second exhaust means 36 and the steel plate outlet 35). A partition 39 including partition walls 37 and 38 that are paired up and down to suppress outflow of combustion exhaust gas in the fire-type heating furnace 14 is provided. Here, the second exhaust means 36 is connected to an intermediate portion of the ceiling of the steel plate outlet portion 35 and exhaust gas exhaust duct 40 for exhausting the combustion exhaust gas in the steel plate outlet portion 35, and a second exhaust gas exhaust duct 40 connected to the exhaust gas exhaust duct 40. The chimney 41 is provided. The exhaust gas discharge duct 40 is provided with a third damper 42. Thereby, it is possible to prevent the combustion exhaust gas from flowing out to the subsequent stage of the direct-fired heating furnace 14.

続いて、本発明の一実施の形態に係る塗装鋼板の連続処理装置10の作用について説明する。
図2に示すように、ラジアントチューブ炉12内が600〜1000℃に、直火式加熱炉14内が800〜1200℃となるように、ラジアントチューブ炉12のラジアントチューブ及び直火式加熱炉14のバーナを使用する場合、第1の排気手段16の燃焼排ガス排出ダクト24の第1のダンパ27、ダクト26の第2のダンパ28、及び第2の排気手段36の排ガス排出ダクト40の第3のダンパ42をそれぞれ開にすると、直火式加熱炉14の鋼板出口部35には燃焼排ガスの流出を抑制する仕切り39が設けられているので、第1の煙突25のドラフト効果により直火式加熱炉14で発生した燃焼排ガスの大半は、直火式加熱炉14からラジアントチューブ炉12内に流入し、ラジアントチューブ炉12の上流側(鋼板入口15)に向けて流れる。
Then, the effect | action of the continuous processing apparatus 10 of the coated steel plate which concerns on one embodiment of this invention is demonstrated.
As illustrated in FIG. 2, the radiant tube furnace 12 and the direct-fired heating furnace 14 are configured so that the inside of the radiant tube furnace 12 is 600 to 1000 ° C. and the inside of the direct-fired heating furnace 14 is 800 to 1200 ° C. When the second burner is used, the first damper 27 of the combustion exhaust gas exhaust duct 24 of the first exhaust means 16, the second damper 28 of the duct 26, and the third of the exhaust gas exhaust duct 40 of the second exhaust means 36 are used. When each of the dampers 42 is opened, a partition 39 for suppressing the outflow of the combustion exhaust gas is provided at the steel plate outlet 35 of the direct-fired heating furnace 14, so that the direct-fire type is achieved by the draft effect of the first chimney 25. Most of the combustion exhaust gas generated in the heating furnace 14 flows into the radiant tube furnace 12 from the direct-fired heating furnace 14 and enters the upstream side of the radiant tube furnace 12 (steel plate inlet 15). Only it flows.

このため、ラジアントチューブ炉12内を通過する塗装膜が塗布された鋼板11は、ラジアントチューブ炉12内に流入した燃焼排ガスにより加熱され、ラジアントチューブ炉12の燃料原単位が低減してラジアントチューブ炉12の熱効率が向上する。そして、ラジアントチューブ炉12の上流側に移動した燃焼排ガスの一部は、ダクト26内に進入し第1の煙突25から排出される。 For this reason, the steel plate 11 coated with the coating film passing through the radiant tube furnace 12 is heated by the combustion exhaust gas flowing into the radiant tube furnace 12, and the fuel intensity of the radiant tube furnace 12 is reduced, thereby reducing the radiant tube furnace. The thermal efficiency of 12 is improved. A part of the combustion exhaust gas that has moved to the upstream side of the radiant tube furnace 12 enters the duct 26 and is discharged from the first chimney 25.

また、ラジアントチューブ炉12の鋼板入口15の直上流側(外側)の上方には、第1の煙突25と連通している燃焼排ガス排出ダクト24の吸引口が配置されているので、第1の煙突25のドラフト効果により燃焼排ガスの残部は燃焼排ガス排出ダクト24で吸引されて第1の煙突25から排出される。例えば、直火式加熱炉自体から250Nm/hrの流量で燃焼排ガスを排出し、ラジアントチューブ炉の鋼板入口の下部から800Nm/hrの流量で外気が流入し、ラジアントチューブ炉の鋼板入口の上部から550Nm/hrの流量で外気が流出していた従来の塗装鋼板の連続処理装置と比べ、本発明ではラジアントチューブ炉12の鋼板入口15の下部から800Nm/hrの流量で外気が流入し、ラジアントチューブ炉12の鋼板入口15の上部より800Nm/hrの流量で外気が流出した場合、例えば、ラジアントチューブ炉12の炉幅が1.5mであると、鋼板入口15の開口部高さ(上仕切り部材21の下端面と下仕切り部材22の上端面との距離)を340mmから390mm(15%)に拡げることが可能になった。なお、直火式加熱炉14で発生した燃焼排ガスの一部は、仕切り39を介して直火式加熱炉14の鋼板出口部35内にも漏れ出すが、鋼板出口部35内に漏れ出した燃焼排ガスは第2の煙突41のドラフト効果により排ガス排出ダクト40で吸引されて第2の煙突41から排出される。このため、直火式加熱炉14の後段(炉内ロール43側)に燃焼排ガスが流出することが防止できる。 Moreover, since the suction port of the combustion exhaust gas discharge duct 24 communicating with the first chimney 25 is disposed above the upstream side (outside) of the steel plate inlet 15 of the radiant tube furnace 12, the first Due to the draft effect of the chimney 25, the remainder of the combustion exhaust gas is sucked in the combustion exhaust gas discharge duct 24 and discharged from the first chimney 25. For example, a direct-fired heating furnace itself emit combustion exhaust gas at a flow rate of 250 Nm 3 / hr, from the bottom of the steel sheet inlet of the radiant tube furnace ambient air flows at a flow rate of 800 Nm 3 / hr, the steel sheet inlet of radiant tube furnace Compared with the conventional coated steel sheet continuous processing apparatus in which the outside air flows out from the upper part at a flow rate of 550 Nm 3 / hr, in the present invention, the outside air flows in from the lower part of the steel sheet inlet 15 of the radiant tube furnace 12 at a flow rate of 800 Nm 3 / hr. When the outside air flows out from the upper part of the steel plate inlet 15 of the radiant tube furnace 12 at a flow rate of 800 Nm 3 / hr, for example, if the furnace width of the radiant tube furnace 12 is 1.5 m, the opening height of the steel plate inlet 15 (The distance between the lower end surface of the upper partition member 21 and the upper end surface of the lower partition member 22) can be increased from 340 mm to 390 mm (15%). It became possible. A part of the flue gas generated in the direct-fired heating furnace 14 leaks into the steel plate outlet 35 of the direct-fired heating furnace 14 through the partition 39, but leaks into the steel plate outlet 35. The combustion exhaust gas is sucked by the exhaust gas exhaust duct 40 due to the draft effect of the second chimney 41 and discharged from the second chimney 41. For this reason, it is possible to prevent the combustion exhaust gas from flowing out to the subsequent stage (inside the furnace roll 43 side) of the direct-fired heating furnace 14.

直火式加熱炉14の燃焼負荷が低下し、燃焼排ガスの発生量が減少しても、塗装鋼板の連続処理装置10においては、直火式加熱炉14自体に煙突と連通する連結管を設けておらず、直火式加熱炉14の上流側に隣接するラジアントチューブ炉12の鋼板入口15の前後に第1の煙突25に連通する燃焼排ガス排出ダクト24及びダクト26を設けている。このため、直火式加熱炉14の燃焼負荷低下時においてもラジアントチューブ炉12内には下流側から上流側に向かう燃焼排ガスの流れが存在している。この流れによって外気が更にラジアントチューブ炉12の深部に向けて侵入するのが抑制され、侵入した外気は燃焼排ガスと共にダクト26で吸引されて第1の煙突25から排出される。 Even if the combustion load of the direct-fired heating furnace 14 is reduced and the generation amount of combustion exhaust gas is reduced, the continuous processing apparatus 10 for coated steel sheets is provided with a connecting pipe communicating with the chimney in the direct-fired heating furnace 14 itself. In addition, a flue gas exhaust duct 24 and a duct 26 communicating with the first chimney 25 are provided before and after the steel plate inlet 15 of the radiant tube furnace 12 adjacent to the upstream side of the direct heating furnace 14. For this reason, even when the combustion load of the direct heating furnace 14 is reduced, a flow of combustion exhaust gas from the downstream side to the upstream side exists in the radiant tube furnace 12. This flow prevents the outside air from further entering into the deep portion of the radiant tube furnace 12, and the outside air that has entered is sucked together with the combustion exhaust gas by the duct 26 and is discharged from the first chimney 25.

このため、直火式加熱炉自体に煙突と連通する連結管を設けている従来技術では、ラジアントチューブ炉12の深部に向けて外気が侵入するのを抑制するため、鋼板入口から燃焼排ガスを流出させることが可能となる燃焼排ガス量の発生を確保する必要があり直火式加熱炉の燃焼負荷を低下することができなかったが、塗装鋼板の連続処理装置10では、直火式加熱炉14の燃焼負荷を低下させてもラジアントチューブ炉12内の下流側から上流側に向かう燃焼排ガスの流れでラジアントチューブ炉12内に侵入した外気が更にラジアントチューブ炉12の深部に向けて侵入するのが抑制されるので、直火式加熱炉14の燃焼負荷を低下することが可能になる。その結果、直火式加熱炉14における上限温度の制約が厳しい鋼板11の処理を行うことが可能になる。
水溶性の塗装膜の乾燥及び焼付けに本実施の形態の塗装鋼板の連続処理装置を適用する場合、塗装膜中の溶媒が突沸し易い水溶性の塗装膜であっても、溶媒の突沸を防止でき、色むらの発生を抑えた品質の高い塗装膜を備えた塗装鋼板を得ることができる。
また、方向性珪素鋼板の絶縁皮膜の乾燥及び焼付けに本実施の形態の塗装鋼板の連続処理装置を適用する場合、ラジアントチューブ炉12の鋼板入口15の扉23に方向性珪素鋼板が接触することがなく、方向性珪素鋼板と扉23との接触により絶縁皮膜に疵が入り絶縁が破壊されるのを防止でき、均一な特性の絶縁皮膜を確保できる。
For this reason, in the conventional technology in which the direct-fired heating furnace itself is provided with a connecting pipe communicating with the chimney, in order to suppress the intrusion of outside air toward the deep part of the radiant tube furnace 12, the combustion exhaust gas flows out from the steel plate inlet. Although it was necessary to ensure the generation of the amount of combustion exhaust gas that can be generated, the combustion load of the direct-fired heating furnace could not be reduced. Even if the combustion load of the radiant tube furnace 12 is reduced, the outside air that has entered the radiant tube furnace 12 due to the flow of the combustion exhaust gas flowing from the downstream side to the upstream side in the radiant tube furnace 12 further enters the deep portion of the radiant tube furnace 12. Since it is suppressed, it becomes possible to reduce the combustion load of the direct-fired heating furnace 14. As a result, it becomes possible to process the steel plate 11 with severe restrictions on the upper limit temperature in the direct-fired heating furnace 14.
When applying the continuous processing equipment for coated steel sheets according to this embodiment to dry and bake water-soluble coating film, even if the solvent in the coating film is water-soluble coating film, it can prevent solvent boiling It is possible to obtain a coated steel sheet provided with a high-quality coating film that suppresses the occurrence of uneven color.
Moreover, when applying the continuous processing apparatus of the coated steel plate of this Embodiment for drying and baking of the insulating film of a directional silicon steel plate, a directional silicon steel plate contacts the door 23 of the steel plate inlet 15 of the radiant tube furnace 12. In other words, the contact between the grain-oriented silicon steel sheet and the door 23 can prevent the insulation film from wrinkling and destroying the insulation, thereby ensuring an insulation film with uniform characteristics.

以上、本発明を具体化した実施の形態では、図1、図2に示すように、ラジアントチューブ炉12の鋼板出口部13に上、下内面の間隔が狭まった領域を設けて、ラジアントチューブ炉12と直火式加熱炉14との間に境のある実施の形態を示したが、鋼板出口部13に上、下内面の間隔が狭まった領域を設けず、ラジアントチューブ炉12と直火式加熱炉14との間に境が存在しない実施の形態も本発明に含まれる。また、本発明は何ら上記した実施の形態に記載した構成に限定されるものではなく、特許請求の範囲に記載されている事項の範囲内で考えられるその他の実施の形態や変形例も含むものである。 As described above, in the embodiment embodying the present invention, as shown in FIGS. 1 and 2, the steel tube outlet portion 13 of the radiant tube furnace 12 is provided with a region where the space between the upper and lower inner surfaces is narrowed, thereby providing the radiant tube furnace. Although the embodiment with a boundary between the direct-fired heating furnace 14 and the direct-fired heating furnace 14 is shown, a region where the distance between the upper and lower inner surfaces is narrowed is not provided in the steel plate outlet 13, and the radiant tube furnace 12 and the direct-fired heating furnace 14. Embodiments in which no boundary exists with the heating furnace 14 are also included in the present invention. Further, the present invention is not limited to the configurations described in the above-described embodiments, and includes other embodiments and modifications that can be considered within the scope of the matters described in the claims. .

本発明による方向性珪素鋼板の絶縁皮膜の乾燥及び焼付け装置に適用される一実施の形態に係る塗装鋼板の連続処理装置の説明図である。It is explanatory drawing of the continuous processing apparatus of the coated steel plate which concerns on one Embodiment applied to the drying and baking apparatus of the insulating film of the grain-oriented silicon steel plate by this invention. 同塗装鋼板の連続処理装置の作用の説明図である。It is explanatory drawing of an effect | action of the continuous processing apparatus of the same coated steel plate.

符号の説明Explanation of symbols

10:塗装鋼板の連続処理装置、11:鋼板、12:ラジアントチューブ炉、13:鋼板出口部、14:直火式加熱炉、15:鋼板入口、16:第1の排気手段、17:コーターロール、18:支持ロール、19:乾燥処理部、20:排出ロール、21:上仕切り部材、22:下仕切り部材、23:扉、24:燃焼排ガス排出ダクト、25:第1の煙突、26:ダクト、27:第1のダンパ、28:第2のダンパ、29:フード、30:鋼板入口、31:支持ロール、32;焼付け処理部、34:排出ロール、35:鋼板出口部、36:第2の排気手段、37、38:仕切り壁、39:仕切り、40:排ガス排出ダクト、41:第2の煙突、42:第3のダンパ、43:炉内ロール 10: Continuous treatment equipment for coated steel plate, 11: Steel plate, 12: Radiant tube furnace, 13: Steel plate outlet, 14: Direct-fired heating furnace, 15: Steel plate inlet, 16: First exhaust means, 17: Coater roll , 18: support roll, 19: drying processing unit, 20: discharge roll, 21: upper partition member, 22: lower partition member, 23: door, 24: combustion exhaust gas discharge duct, 25: first chimney, 26: duct , 27: first damper, 28: second damper, 29: hood, 30: steel plate inlet, 31: support roll, 32: baking processing unit, 34: discharge roll, 35: steel plate outlet, 36: second Exhaust means, 37, 38: partition wall, 39: partition, 40: exhaust gas exhaust duct, 41: second chimney, 42: third damper, 43: in-furnace roll

Claims (5)

塗装された鋼板が供給されて該鋼板の塗装膜を乾燥する横型カテナリー式のラジアントチューブ炉と、該ラジアントチューブ炉の鋼板出口部に直結し、該ラジアントチューブ炉から排出された前記鋼板を受入れて乾燥後の前記塗装膜を該鋼板に焼付ける直火式加熱炉とを備えた塗装鋼板の連続処理装置において、
前記ラジアントチューブ炉の鋼板入口の直上流側に、前記直火式加熱炉で発生した燃焼排ガスを排気する第1の排気手段を設けたことを特徴とする塗装鋼板の連続処理装置。
A horizontal catenary-type radiant tube furnace that is supplied with a coated steel sheet and dries the coated film of the steel sheet, and is directly connected to a steel sheet outlet of the radiant tube furnace, and accepts the steel sheet discharged from the radiant tube furnace. In a continuous processing apparatus for a coated steel sheet, comprising a direct-fired heating furnace for baking the coated film after drying to the steel sheet,
A continuous processing apparatus for coated steel sheets, wherein a first exhaust means for exhausting combustion exhaust gas generated in the direct-fired heating furnace is provided immediately upstream of the steel sheet inlet of the radiant tube furnace.
請求項1記載の塗装鋼板の連続処理装置において、前記ラジアントチューブ炉の前記鋼板入口の直下流側に、前記第1の排気手段と連通し該鋼板入口から侵入した外気を吸引するダクトを設けたことを特徴とする塗装鋼板の連続処理装置。 The continuous processing apparatus for coated steel sheets according to claim 1, wherein a duct is provided on the downstream side of the steel sheet inlet of the radiant tube furnace to communicate with the first exhaust means and suck outside air that has entered from the steel sheet inlet. The continuous processing apparatus of the coated steel plate characterized by the above-mentioned. 請求項1及び2のいずれか1項に記載の塗装鋼板の連続処理装置において、前記直火式加熱炉の鋼板出口部に該鋼板出口部に連通し該鋼板出口部内の燃焼排ガスを排気する第2の排気手段を設け、該第2の排気手段と該鋼板出口部との連通部の直上流側の該鋼板出口部の部位に前記鋼板を通過させ該直火式加熱炉内の燃焼排ガスの流出を抑制する仕切りを設けたことを特徴とする塗装鋼板の連続処理装置。 The continuous processing apparatus of the coated steel plate of any one of Claim 1 and 2 WHEREIN: It communicates with this steel plate exit part in the steel plate exit part of the said direct-fired heating furnace, and exhausts the combustion exhaust gas in this steel plate exit part. 2 is provided, and the steel plate is passed through a portion of the steel plate outlet portion immediately upstream of the communication portion between the second exhaust means and the steel plate outlet portion. A continuous processing apparatus for coated steel sheets, characterized in that a partition for suppressing outflow is provided. 請求項1〜3のいずれか1項に記載の塗装鋼板の連続処理装置において、該塗装鋼板の連続処理装置を水溶性の塗装膜の乾燥及び焼付け装置とすることを特徴とする塗装鋼板の連続処理装置。 The continuous processing apparatus for coated steel sheets according to any one of claims 1 to 3, wherein the continuous processing apparatus for coated steel sheets is a water-soluble coating film drying and baking apparatus. Processing equipment. 請求項4記載の塗装鋼板の連続処理装置において、前記水溶性の塗装膜は方向性珪素鋼板の絶縁皮膜であることを特徴とする塗装鋼板の連続処理装置。 The continuous processing apparatus for coated steel sheets according to claim 4, wherein the water-soluble coating film is an insulating film of a directional silicon steel sheet.
JP2008285820A 2008-11-06 2008-11-06 Continuous processing equipment for painted steel sheet Expired - Fee Related JP5192988B2 (en)

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JPS5996227A (en) * 1982-11-24 1984-06-02 Kawasaki Steel Corp Continuous annealing installation for silicon steel plate
JPH0184774U (en) * 1987-11-27 1989-06-06
JPH04219171A (en) * 1990-12-19 1992-08-10 Kawasaki Steel Corp Furnace for continuously drying and baking coated metal strip
JPH10239160A (en) * 1997-02-24 1998-09-11 Nippon Steel Corp Method and device for measuring plate temperature of continuous type drying and baking oven

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