JP2001098320A - Control method of furnace pressure in heating furnace - Google Patents
Control method of furnace pressure in heating furnaceInfo
- Publication number
- JP2001098320A JP2001098320A JP27161899A JP27161899A JP2001098320A JP 2001098320 A JP2001098320 A JP 2001098320A JP 27161899 A JP27161899 A JP 27161899A JP 27161899 A JP27161899 A JP 27161899A JP 2001098320 A JP2001098320 A JP 2001098320A
- Authority
- JP
- Japan
- Prior art keywords
- furnace
- furnace pressure
- gas
- heating furnace
- heating
- 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
- Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、加熱炉の炉圧制御
方法に係わり、特に、蓄熱体を有する交番燃焼バーナを
備えた加熱炉の炉圧を制御する技術に関する。The present invention relates to a furnace pressure control method for a heating furnace, and more particularly to a technique for controlling the furnace pressure of a heating furnace provided with an alternating combustion burner having a heat storage body.
【0002】[0002]
【従来の技術】例えば、鋼材の加熱に、回転式の加熱炉
が使用されることがある。それは、図4に示すように、
平面がドーナツ状を呈する炉室1と、回転する水平な炉
床2と、被加熱物3を加熱するバーナ4とで形成されて
いる。この炉を使用すると、装入口5から入れられた被
加熱物3は、炉内を排出口6まで移動する間に、炉床2
の回転速度と炉内温度を適当に調整することで所望温度
に加熱される。バーナ4は、一般に重油バーナが用いら
れ、炉室1の両側壁(ドーナツ状なので、直径の小さい
方を内側壁7、大きい方を外側壁8という)に沿って、
その先端を炉内へ向けて多数配設されている。かかる加
熱炉を実際に稼動させるには、高温排ガスの熱をレキュ
ペレータ9で燃焼に用いる空気と熱交換したり、図3
(a)に示すように予熱炉10や廃熱ボイラ11で回収
して、熱効率を高めるようにしていた。それでも、該加
熱炉は、炉体の構造上、炉容積に対して表面積が大き
く、熱交換を利用しても燃焼効率が悪く、必然的に燃料
原単位が高いという問題があった。また、被加熱物3が
鋼材の場合、加熱中に酸化されてスケールが生じ、所謂
スケールロスが大きいという問題もあった。2. Description of the Related Art For example, a rotary heating furnace is sometimes used for heating steel materials. It is, as shown in FIG.
The furnace chamber 1 has a doughnut-shaped plane, a rotating horizontal hearth 2, and a burner 4 for heating an object 3 to be heated. When this furnace is used, the object 3 to be heated entered through the charging port 5 moves through the furnace to the discharge port 6 while the furnace floor 2
The temperature is heated to a desired temperature by appropriately adjusting the rotation speed and the furnace temperature. As the burner 4, a heavy oil burner is generally used, and along the both side walls of the furnace chamber 1 (doughnut-shaped, the smaller diameter is called the inner wall 7 and the larger diameter is called the outer wall 8).
Many are arranged with their tips facing the furnace. In order to actually operate such a heating furnace, the heat of the high-temperature exhaust gas is exchanged with the air used for combustion by the recuperator 9 or as shown in FIG.
As shown in (a), the heat is recovered by the preheating furnace 10 and the waste heat boiler 11 to increase the thermal efficiency. Nevertheless, due to the structure of the furnace, the heating furnace has a problem that the surface area is large with respect to the furnace volume, the combustion efficiency is low even when heat exchange is used, and the fuel consumption rate is necessarily high. Further, when the object to be heated 3 is a steel material, it is oxidized during heating to produce scale, and there is a problem that so-called scale loss is large.
【0003】これに対して、特開平7−4851号公報
は、それぞれ蓄熱体を備えた2つのバーナを1組とし、
交互に切換えて燃焼、吸引をする交番燃焼バーナを、前
記内側壁や天井面に沿って複数組配置する加熱炉を提案
している。この炉では、排気ガスの熱量をほとんど自ら
のバーナ(蓄熱体)で回収するようにしたので、熱効率
が従来に比べて大きくなる。また、重油の予熱器や熱交
換器のような大型設備が不要となり、建設費も安くな
る。さらに、鋼材のスケールが低減するという効果もあ
る程度認められた。On the other hand, Japanese Patent Application Laid-Open No. 7-4851 discloses a set of two burners each having a heat storage body.
A heating furnace has been proposed in which a plurality of sets of alternating combustion burners that alternately switch between combustion and suction are arranged along the inner wall and the ceiling surface. In this furnace, the calorific value of the exhaust gas is mostly recovered by its own burner (heat accumulator), so that the thermal efficiency is higher than in the past. Also, large equipment such as a heavy oil preheater or heat exchanger is not required, and construction costs are reduced. Further, the effect of reducing the scale of the steel material was also recognized to some extent.
【0004】ところで、このような交番燃焼バーナを設
けた加熱炉は、前記従来の炉(図3(a)参照)と異な
り、図3(b)に示すように、熱回収の都合で燃焼ガス
の一部(全体の20vol%と少ない流量である)を直
接煙突15から外気中へ排出させている。従って、炉の
排気口16から煙突15までの煙道17には、図2に示
すように、炉圧を制御するダンパが設けられる。ところ
が、この炉圧制御用ダンパは、一般に密閉性が低いの
で、ガス流量が少ないと、炉圧制御を困難にすることが
ある。つまり、炉圧制御用ダンパ18を密閉しても、該
ダンパ18を通過する排気ガス19の圧力損失が後流側
の圧力(負圧)より小さく、排気ガス19が後流側に流
れてしまうからである。[0004] By the way, the heating furnace provided with such an alternating combustion burner is different from the conventional furnace (see FIG. 3 (a)), and as shown in FIG. (A flow rate as low as 20 vol% of the whole) is directly discharged from the chimney 15 into the outside air. Accordingly, as shown in FIG. 2, a damper for controlling the furnace pressure is provided in the flue 17 from the exhaust port 16 of the furnace to the chimney 15. However, since the furnace pressure control damper generally has low hermeticity, if the gas flow rate is small, the furnace pressure control may be difficult. That is, even if the furnace pressure control damper 18 is sealed, the pressure loss of the exhaust gas 19 passing through the damper 18 is smaller than the pressure (negative pressure) on the downstream side, and the exhaust gas 19 flows on the downstream side. Because.
【0005】[0005]
【発明が解決しようとする課題】本発明は、かかる事情
に鑑み、蓄熱体を有する交番燃焼バーナを備えていて
も、炉圧制御が安定して実施可能な加熱炉の炉圧制御方
法を提供することを目的としている。SUMMARY OF THE INVENTION In view of the above circumstances, the present invention provides a furnace pressure control method for a heating furnace in which furnace pressure control can be stably performed even if an alternating combustion burner having a heat storage body is provided. It is intended to be.
【0006】[0006]
【課題を解決するための手段】発明者は、上記目的を達
成するため鋭意研究し、その成果を本発明に具現化し
た。Means for Solving the Problems The inventor has conducted intensive studies to achieve the above object and has embodied the results in the present invention.
【0007】すなわち、本発明は、蓄熱体を有する交番
燃焼バーナを備えた加熱炉の炉圧を、排ガスの煙道に設
けたダンパの開閉で制御するに際して、前記ダンパの上
流及び/又は下流側で煙道内に低温ガスを導入すること
を特徴とする加熱炉の炉圧制御方法である。That is, according to the present invention, when controlling the furnace pressure of a heating furnace provided with an alternating combustion burner having a heat storage body by opening and closing a damper provided in an exhaust gas flue, the upstream and / or downstream side of the damper And introducing a low-temperature gas into the flue.
【0008】また、本発明は、前記低温ガスを外気とす
ることを特徴とする加熱炉の炉圧制御方法である。Further, the present invention is a furnace pressure control method for a heating furnace, wherein the low-temperature gas is used as outside air.
【0009】さらに、前記外気の導入を、ファンを使用
しない自然吸引とすることを特徴とする加熱炉の炉圧制
御方法である。Further, there is provided a furnace pressure control method for a heating furnace, wherein the outside air is introduced by natural suction without using a fan.
【0010】本発明では、炉から煙突までの煙道に設け
た前記ダンパの上流及び/又は下流側で、該煙道内に低
温ガスを導入するようにしたので、煙道内のガス温度が
低下し、煙突でガスが上昇する速度が低下する(所謂
「ドラフト」が減少する。)。また、ガス圧力も上昇す
る。その結果、ダンパ密閉時に該ダンパを通過して排出
されるガス量が極めて微量に抑えられるようになり、炉
圧の制御が容易になる。さらに、本発明では、低温ガス
を外気とし、該外気の導入を無動力で行なうようにした
ので、炉圧制御が安価に行なえるようになる。In the present invention, a low-temperature gas is introduced into the flue upstream and / or downstream of the damper provided in the flue from the furnace to the chimney, so that the gas temperature in the flue decreases. The speed at which the gas rises in the chimney decreases (so-called "draft" decreases). Also, the gas pressure increases. As a result, the amount of gas discharged through the damper when the damper is closed can be suppressed to a very small amount, and the furnace pressure can be easily controlled. Further, in the present invention, the low-temperature gas is used as outside air, and the introduction of the outside air is performed without power, so that furnace pressure control can be performed at low cost.
【0011】[0011]
【発明の実施の形態】以下、発明をなすに至った経緯も
交え、本発明の実施の形態について説明する。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, embodiments of the present invention will be described with reference to the circumstances leading to the invention.
【0012】まず、発明者は、密閉性の低い炉圧制御ダ
ンパ自体の改造をせずに、前記ドラフトを減少させるこ
とに着眼し、その具体的手段を鋭意検討した。その結
果、排気ガス19の温度を下げること、及び圧力を高め
ることが良いと考えた。具体的には、排気ガス19より
低温のガスを煙道17に導入することである。First, the inventor focused on reducing the draft without remodeling the furnace pressure control damper having a low hermeticity itself, and intensively studied specific means. As a result, the inventors considered that it is better to lower the temperature of the exhaust gas 19 and increase the pressure. Specifically, a gas whose temperature is lower than that of the exhaust gas 19 is introduced into the flue 17.
【0013】導入する低温ガス20の種類は、高温(1
000℃程度)の排気ガス19(交番燃焼バーナからの
燃焼ガスの一部)の成分と反応し、環境汚染や煙道17
を腐食させることを配慮すると、不活性ガスの利用が好
ましい。しかし、発明者の調査により、温度としては、
常温で良く、ガスとしては空気で煙道17に何らトラブ
ルが生じないことが確認できたので、常温の外気が最も
好ましい。また、導入する手段は、不活性ガスの場合に
は、公知のガス保持容器と加圧手段(いずれも図示せ
ず)を設ければ良い。一方、外気の場合には、図1に示
すように、煙道17に外気の取入れ口24とダンパ(以
下、ドラフト制御ダンパ21という)を設けるだけで十
分であった。コンプレッサ等の動力源を使用しても良い
が、煙道17の内部は通常負圧なので、十分な量の外気
が導入できるからである。The type of the low-temperature gas 20 to be introduced is a high-temperature (1
Reacts with components of the exhaust gas 19 (a part of the combustion gas from the alternating combustion burner) of about 000 ° C.
The use of an inert gas is preferred in consideration of corrosion of the steel. However, according to the inventors' research, the temperature was
Room temperature is sufficient, and it has been confirmed that air does not cause any trouble in the flue gas 17 as the gas, so that room temperature outside air is most preferable. In the case of introducing an inert gas, a known gas holding container and a pressurizing means (both not shown) may be provided. On the other hand, in the case of outside air, as shown in FIG. 1, it was sufficient to provide the outside air intake 24 and the damper (hereinafter, referred to as the draft control damper 21) in the flue 17. Although a power source such as a compressor may be used, a sufficient amount of outside air can be introduced because the inside of the flue 17 is usually under negative pressure.
【0014】次に、発明者は、低温ガス20の導入位置
について検討し、前記炉圧制御ダンパ18の上流及び下
流側のいずれでも良いことを知った。いずれ側に導入し
ても、排気ガス19の温度低下及び圧力上昇に寄与する
からである。Next, the inventor examined the introduction position of the low-temperature gas 20 and found that either the upstream or downstream side of the furnace pressure control damper 18 may be used. This is because the introduction to either side contributes to a decrease in the temperature and a rise in the pressure of the exhaust gas 19.
【0015】なお、本発明を具体的に実施するには、オ
ペレータが炉に設けた圧力センサ22を常時監視し、圧
力値が目標圧力範囲内になるように、ドラフト制御ダン
パ21を開閉操作することで、低温ガス20の導入を行
なえば良い。しかし、オペレータをコンピュータに代
え、無人の遠隔操作でドラフト制御ダンパ21の開閉を
行なうようにしても良い。In order to specifically implement the present invention, the operator constantly monitors the pressure sensor 22 provided in the furnace, and opens and closes the draft control damper 21 so that the pressure value falls within a target pressure range. Thus, the low-temperature gas 20 may be introduced. However, the operator may be replaced with a computer, and the draft control damper 21 may be opened and closed by an unattended remote operation.
【0016】[0016]
【実施例】蓄熱体を有する交番燃焼バーナ23を27組
備えた加熱炉(外側壁の直径33m,内側壁の直径25
m,炉床から天井までの高さ1.5〜2.1m)の炉圧
制御に本発明を適用した。被加熱物3は、継目無鋼管を
製造する素材の丸鋼鋳片(1本が外径190mm,長さ
3000mm)であり、それを装入口5から連続的に装
入して加熱操業が行なわれた。該鋳片の目標加熱温度
は、1250±30℃とし、目標炉圧は、20±2Pa
とした。この炉圧制御は、本発明に係る方法のうち、外
気の導入を無人で行なう方式とした。DESCRIPTION OF THE PREFERRED EMBODIMENTS A heating furnace equipped with 27 sets of alternating combustion burners 23 having a heat storage body (the outer wall diameter is 33 m, the inner wall diameter is 25 mm)
m, the height from the hearth to the ceiling is 1.5 to 2.1 m). The object to be heated 3 is a round steel slab (one of which has an outer diameter of 190 mm and a length of 3000 mm) of a material for producing a seamless steel pipe, which is continuously charged from the charging port 5 to perform a heating operation. Was. The target heating temperature of the slab is 1250 ± 30 ° C., and the target furnace pressure is 20 ± 2 Pa
And This furnace pressure control is a method according to the present invention in which outside air is introduced unattended.
【0017】加熱操業中の炉圧の経時変化を、従来の操
業時での変化と比較して図5に示す。図5より、本発明
によれば、炉圧が目標範囲内で制御できることが明らか
である。また、この操業中に加熱された鋳片は、いずれ
も目標加熱温度を満足していた。FIG. 5 shows the change over time of the furnace pressure during the heating operation in comparison with the change during the conventional operation. From FIG. 5, it is clear that according to the present invention, the furnace pressure can be controlled within the target range. The slabs heated during this operation all satisfied the target heating temperature.
【0018】[0018]
【発明の効果】以上述べたように、本発明により、蓄熱
体を有する交番燃焼バーナを備えていても、加熱炉の炉
圧制御が安定して実施できるようになった。しかも、制
御に用いるガスが外気で良いので、簡単な設備改造で安
価に炉圧の安定が図れた。As described above, according to the present invention, even if an alternating combustion burner having a heat storage body is provided, the furnace pressure of the heating furnace can be stably controlled. In addition, since the gas used for the control can be the outside air, the furnace pressure can be stabilized at low cost with simple equipment modification.
【図1】本発明に係る加熱炉の炉圧制御方法を説明する
図である。FIG. 1 is a diagram illustrating a furnace pressure control method for a heating furnace according to the present invention.
【図2】交番燃焼バーナを備えた加熱炉の排気系を示す
図である。FIG. 2 is a view showing an exhaust system of a heating furnace provided with an alternating combustion burner.
【図3】従来の加熱炉の排気系を説明する図であり、
(a)はバーナが重油バーナ、(b)は交番燃焼バーナ
の場合である。FIG. 3 is a diagram illustrating an exhaust system of a conventional heating furnace.
(A) shows the case where the burner is a heavy oil burner, and (b) shows the case where the burner is an alternating combustion burner.
【図4】加熱炉の構造を説明する図である。FIG. 4 is a diagram illustrating the structure of a heating furnace.
【図5】本発明の実施による炉圧変化を、従来のものと
比較した図である。FIG. 5 is a diagram comparing a furnace pressure change according to an embodiment of the present invention with a conventional furnace pressure change.
1 炉室 2 炉床 3 被加熱物 4 バーナ 5 装入口 6 排出口 7 内側壁 8 外側壁 9 レキュペレータ 10 予熱炉 11 廃熱ボイラ 12 燃焼ブロア 13 排気ブロア 14 高温ファン 15 煙突 16 炉の排気口 17 煙道 18 炉圧制御ダンパ 19 排気ガス(燃焼ガスの一部) 20 低温ガス 21 ドラフト制御ダンパ 22 圧力センサ 23 交番燃焼バーナ 24 外気の取り入れ口 DESCRIPTION OF SYMBOLS 1 Furnace room 2 Hearth 3 Heated object 4 Burner 5 Inlet 6 Outlet 7 Inner wall 8 Outer side wall 9 Recuperator 10 Preheating furnace 11 Waste heat boiler 12 Combustion blower 13 Exhaust blower 14 High temperature fan 15 Chimney 16 Furnace exhaust port 17 Flue gas 18 Furnace pressure control damper 19 Exhaust gas (part of combustion gas) 20 Low temperature gas 21 Draft control damper 22 Pressure sensor 23 Alternating combustion burner 24 External air intake
Claims (3)
加熱炉の炉圧を、排ガスの煙道に設けたダンパの開閉で
制御するに際して、 前記ダンパの上流及び/又は下流側で煙道内に低温ガス
を導入することを特徴とする加熱炉の炉圧制御方法。When controlling a furnace pressure of a heating furnace provided with an alternating combustion burner having a heat accumulator by opening and closing a damper provided in a flue of exhaust gas, the furnace pressure is set in a flue upstream and / or downstream of the damper. A furnace pressure control method for a heating furnace, characterized by introducing a low-temperature gas.
する請求項1記載の加熱炉の炉圧制御方法。2. The furnace pressure control method for a heating furnace according to claim 1, wherein the low-temperature gas is outside air.
自然吸引とすることを特徴とする請求項2記載の加熱炉
の炉圧制御方法。3. The furnace pressure control method for a heating furnace according to claim 2, wherein the outside air is introduced by natural suction without using a fan.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP27161899A JP3733803B2 (en) | 1999-09-27 | 1999-09-27 | Furnace pressure control method for rotary hearth furnace |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP27161899A JP3733803B2 (en) | 1999-09-27 | 1999-09-27 | Furnace pressure control method for rotary hearth furnace |
Publications (2)
Publication Number | Publication Date |
---|---|
JP2001098320A true JP2001098320A (en) | 2001-04-10 |
JP3733803B2 JP3733803B2 (en) | 2006-01-11 |
Family
ID=17502590
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP27161899A Expired - Fee Related JP3733803B2 (en) | 1999-09-27 | 1999-09-27 | Furnace pressure control method for rotary hearth furnace |
Country Status (1)
Country | Link |
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JP (1) | JP3733803B2 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2002057501A1 (en) * | 2001-01-17 | 2002-07-25 | Kawasaki Steel Corporation | Heating furnace with regenerative burners and method of operating the heating furnace |
JP2015197269A (en) * | 2014-04-02 | 2015-11-09 | 中外炉工業株式会社 | Regenerative burner and combustion furnace with regenerative burner |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US9388991B2 (en) * | 2011-04-27 | 2016-07-12 | Electrolux Home Products, Inc. | Flow control device for an oven |
-
1999
- 1999-09-27 JP JP27161899A patent/JP3733803B2/en not_active Expired - Fee Related
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2002057501A1 (en) * | 2001-01-17 | 2002-07-25 | Kawasaki Steel Corporation | Heating furnace with regenerative burners and method of operating the heating furnace |
US6644962B2 (en) | 2001-01-17 | 2003-11-11 | Kawasaki Steel Corporation | Heating furnace having heat regenerating burners and operation method thereof |
EP1757707A3 (en) * | 2001-01-17 | 2007-06-20 | JFE Steel Corporation | Heating furnace having heat regenerating burners and operation method thereof |
JP2015197269A (en) * | 2014-04-02 | 2015-11-09 | 中外炉工業株式会社 | Regenerative burner and combustion furnace with regenerative burner |
Also Published As
Publication number | Publication date |
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JP3733803B2 (en) | 2006-01-11 |
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