JPH04276013A - Method for operating batch type heating furnace - Google Patents
Method for operating batch type heating furnaceInfo
- Publication number
- JPH04276013A JPH04276013A JP3646791A JP3646791A JPH04276013A JP H04276013 A JPH04276013 A JP H04276013A JP 3646791 A JP3646791 A JP 3646791A JP 3646791 A JP3646791 A JP 3646791A JP H04276013 A JPH04276013 A JP H04276013A
- Authority
- JP
- Japan
- Prior art keywords
- heating furnace
- batch
- steel material
- air ratio
- burning
- 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)
- Heat Treatment Of Strip Materials And Filament Materials (AREA)
Abstract
Description
【0001】0001
【産業上の利用分野】この発明は、バッチ式加熱炉の操
業方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention This invention relates to a method of operating a batch heating furnace.
【0002】0002
【従来の技術】バッチ式加熱炉で鋼材を加熱する場合に
は、空気比m=1.05で、燃焼排ガス中のO2%が1
〜5%前後となるような燃焼雰囲気で加熱するので、鋼
材の表面にスケールが発生したり、結晶粒界が酸化する
等により、歩留が低下するという問題がある。[Prior Art] When heating steel materials in a batch heating furnace, the air ratio m = 1.05 and O2% in the combustion exhaust gas is 1.
Since heating is carried out in a combustion atmosphere where the concentration is around 5%, there is a problem that the yield is reduced due to scale generation on the surface of the steel material, oxidation of grain boundaries, etc.
【0003】0003
【発明が解決しようとする課題】上述したような鋼材の
加熱中の酸化を防止する加熱方法としては、コークス炉
ガスを空気比m=0.45程度で燃焼させた不完全燃焼
雰囲気で加熱する平衡理論直火還元加熱方法がある。し
かしながら、この方法では、鋼材の酸化は抑えられるが
、炉の熱効率が一般加熱炉の60%に対し、約20%と
非常に低く、熱回収設備や安全対策等、設備費が非常に
高くなるという問題点がある。[Problems to be Solved by the Invention] As a heating method for preventing oxidation during heating of steel materials as described above, heating is performed in an incomplete combustion atmosphere in which coke oven gas is combusted at an air ratio m = approximately 0.45. There is an equilibrium theory direct fire reduction heating method. However, although this method suppresses oxidation of steel, the thermal efficiency of the furnace is very low at approximately 20%, compared to 60% for a general heating furnace, and equipment costs such as heat recovery equipment and safety measures are extremely high. There is a problem.
【0004】この発明は、従来技術の上記のような問題
点を解消し、鋼材を酸化させることなく加熱することが
でき、しかも特別な熱回収設備や煙道等の安全対策を必
要としないバッチ式加熱炉の操業方法を提供することを
目的としている。[0004] The present invention solves the above-mentioned problems of the prior art, and is capable of heating steel without oxidizing it, and moreover, it is a batch process that does not require special heat recovery equipment or safety measures such as a flue. The purpose is to provide a method for operating a type heating furnace.
【0005】[0005]
【課題を解決するための手段】この発明に係るバッチ式
加熱炉の操業方法は、2基のバッチ式加熱炉を使用し、
第1のバッチ式加熱炉においては燃料を空気比0.3〜
0.8で燃焼させて鋼材を加熱し、前記第1のバッチ式
加熱炉で発生した燃焼ガスを第1のバッチ式加熱炉と第
2のバッチ式加熱炉を連結するダクトを経由して第2の
バッチ式加熱炉に導入し、第2のバッチ式加熱炉では前
記燃焼ガスを空気比1.0以上で燃焼させて鋼材を加熱
するものである。[Means for Solving the Problems] A method for operating a batch-type heating furnace according to the present invention uses two batch-type heating furnaces,
In the first batch heating furnace, the fuel and air ratio is 0.3~
0.8 to heat the steel material, and the combustion gas generated in the first batch heating furnace is passed through a duct connecting the first batch heating furnace and the second batch heating furnace to the second batch heating furnace. In the second batch heating furnace, the combustion gas is combusted at an air ratio of 1.0 or more to heat the steel material.
【0006】[0006]
【作用】この発明に係るバッチ式加熱炉の操業方法は、
2基のバッチ式加熱炉を使用し、第1のバッチ式加熱炉
においては燃料を空気比0.3〜0.8で燃焼させて鋼
材を加熱し、前記第1のバッチ式加熱炉で発生した燃焼
ガスを第1のバッチ式加熱炉と第2のバッチ式加熱炉を
連結するダクトを経由して第2のバッチ式加熱炉に導入
し、第2のバッチ式加熱炉では前記燃焼ガスを空気比1
.0以上で燃焼させて鋼材を加熱するようにしている。[Operation] The method of operating a batch heating furnace according to the present invention is as follows:
Two batch-type heating furnaces are used; in the first batch-type heating furnace, fuel is burned at an air ratio of 0.3 to 0.8 to heat the steel material; The combustion gas is introduced into the second batch heating furnace through a duct connecting the first batch heating furnace and the second batch heating furnace, and the combustion gas is introduced into the second batch heating furnace. air ratio 1
.. The steel is heated by combustion at temperatures above 0.
【0007】このようにして操業すると、鋼材を酸化さ
せないで加熱することができるとともに、この鋼材の加
熱により発生した未燃焼部分を含んだ燃焼排ガスをアフ
ターバーニングさせて鋼材の余熱に使用するので、炉の
熱効率が低下しない。[0007] When operated in this manner, the steel material can be heated without oxidizing it, and the combustion exhaust gas containing unburned parts generated by heating the steel material is afterburned and used for residual heat of the steel material. Thermal efficiency of the furnace does not decrease.
【0008】また、未燃焼部分を含んだ燃焼排ガスをア
フターバーニングさせて、未燃焼部分を燃焼させてしま
うので、特別な熱回収設備や煙道等の安全対策を必要と
しない。Furthermore, since the combustion exhaust gas containing unburned parts is afterburned and the unburned parts are combusted, safety measures such as special heat recovery equipment and flues are not required.
【0009】なお、第1のバッチ式加熱炉の空気比を0
.3以上としたのは、これ未満では鋼材を加熱するため
の火炎温度が得られないからであり、0.8以下とした
のは、図3に示す空気比とスケール厚み比(空気比1.
1のときのスケール厚みを100%とする)との関係を
示すグラフに見られるように、これ以下であればスケー
ル生成量が急激に低下するからである。[0009] Note that the air ratio in the first batch heating furnace is 0.
.. The reason why it is set to 3 or more is because if it is less than this, the flame temperature for heating the steel material cannot be obtained, and the reason why it is set to 0.8 or less is because the air ratio and scale thickness ratio (air ratio 1.
This is because, as can be seen in the graph showing the relationship between the scale thickness and the scale thickness when the thickness is 100%, if the thickness is less than this, the amount of scale generated will decrease rapidly.
【0010】また、第2のバッチ式加熱炉の空気比を1
.0以上としたのは、アフターバーニングを行なうのが
目的であるので、必然的に1.0以上になるのである。[0010] Furthermore, the air ratio of the second batch type heating furnace is set to 1.
.. The purpose of setting the value to be 0 or more is to perform afterburning, so it is necessarily 1.0 or more.
【0011】[0011]
【実施例】本発明の1実施例のバッチ式加熱炉の操業方
法を図1により説明する。図1は、本発明の1実施例の
バッチ式加熱炉の操業方法を実施する際に使用するバッ
チ式加熱炉の配置を示す配置図である。本発明の1実施
例のバッチ式加熱炉の操業方法においては、第1のバッ
チ式加熱炉1により、酸化させたくない鋼材2を、コー
クス炉ガスをバーナー3により空気比m=0.3〜0.
8で燃焼させた不完全燃焼雰囲気で加熱する。そして、
第1のバッチ式加熱炉1において発生した未燃焼部分を
含んだ燃焼ガス4をダクト9を通して第2のバッチ式加
熱炉5に導入し、この燃焼排ガス4をアフターバーニン
グ用バーナー6によりアフターバーニングさせて、それ
ほど表面の酸化を問題としない鋼材7を予熱する。そし
て、アフターバーニング後の燃焼排ガス8は、煙突を介
して大気中に放散する。[Embodiment] A method of operating a batch type heating furnace according to an embodiment of the present invention will be explained with reference to FIG. FIG. 1 is a layout diagram showing the arrangement of a batch-type heating furnace used when implementing a method for operating a batch-type heating furnace according to an embodiment of the present invention. In the operating method of a batch heating furnace according to one embodiment of the present invention, a steel material 2 that is not to be oxidized is heated in a first batch heating furnace 1, and a coke oven gas is fed into an air ratio m=0.3 to 0.
Heat in the incomplete combustion atmosphere used in step 8. and,
Combustion gas 4 containing an unburned portion generated in the first batch heating furnace 1 is introduced into the second batch heating furnace 5 through a duct 9, and this combustion exhaust gas 4 is subjected to afterburning by an afterburning burner 6. Then, the steel material 7 whose surface oxidation is not a problem is preheated. The combustion exhaust gas 8 after afterburning is then diffused into the atmosphere through the chimney.
【0012】図2のグラフは、第1のバッチ式加熱炉で
の鋼材のスケールロスを示すもので、第1のバッチ式加
熱炉に幅400mm、高さ500mm、長さ4000m
mの重量6トン程度の鋼材を装入して加熱した場合と、
従来法で加熱した場合と比較したものである。従来2%
程度のスケールロスがあったものが、本方法で加熱する
とほとんどスケールロスが発生しないことが分かる。The graph in FIG. 2 shows the scale loss of steel materials in the first batch heating furnace.
When steel material weighing about 6 tons is charged and heated,
This is a comparison with the case of heating using the conventional method. Conventional 2%
It can be seen that when heating with this method, almost no scale loss occurs even though there was some scale loss.
【0013】なお、第2のバッチ式加熱炉でアフターバ
ーニングさせないと、燃料原単位が112×103kc
al/T余分にかかることになる。[0013] If afterburning is not performed in the second batch heating furnace, the fuel consumption rate will be 112 x 103 kc.
It will cost extra al/T.
【0014】本発明の1実施例のバッチ式加熱炉の操業
方法においては、上述のようにして、鋼材を酸化させな
いで加熱できるとともに、この鋼材を加熱した未燃焼部
分を含んだ燃焼ガスをアフターバーニングさせて他の鋼
材を加熱するようにしているので、加熱炉の熱効率は低
下しない。また、未燃焼部分を含んだ燃焼ガスを完全燃
焼させるので、熱回収設備や安全対策を必要としない。[0014] In the operating method of a batch-type heating furnace according to one embodiment of the present invention, as described above, the steel material can be heated without oxidizing it, and the combustion gas containing the unburned portion of the heated steel material can be removed after heating. Since other steel materials are heated by burning, the thermal efficiency of the heating furnace does not decrease. Furthermore, since the combustion gas including the unburned portion is completely combusted, there is no need for heat recovery equipment or safety measures.
【0015】[0015]
【発明の効果】この発明により、加熱炉の熱効率を低下
させず、かつ特別な熱回収設備や安全対策を必要とせず
に、鋼材を酸化させないで加熱することができる。[Effects of the Invention] According to the present invention, it is possible to heat a steel material without oxidizing it without reducing the thermal efficiency of the heating furnace, without requiring special heat recovery equipment or safety measures.
【図1】本発明の1実施例のバッチ式加熱炉の操業方法
を実施する際に使用するバッチ式加熱炉の配置を示す配
置図である。FIG. 1 is a layout diagram showing the arrangement of a batch-type heating furnace used when implementing a method for operating a batch-type heating furnace according to an embodiment of the present invention.
【図2】スケールロスの変化を示すグラフである。FIG. 2 is a graph showing changes in scale loss.
【図3】空気比とスケール厚み比との関係を示すグラフ
である。FIG. 3 is a graph showing the relationship between air ratio and scale thickness ratio.
1 第1の加熱炉 2 鋼材 3 バーナー 4 未燃焼部分を含んだ燃焼排ガス 5 第2の加熱炉 6 アフターバーニング用バーナー 7 鋼材 8 アフターバーニング後の燃焼排ガス9 ダクト 1 First heating furnace 2 Steel material 3 Burner 4 Combustion exhaust gas including unburned parts 5 Second heating furnace 6 Burner for afterburning 7 Steel material 8 Combustion exhaust gas after afterburning 9 Duct
Claims (1)
のバッチ式加熱炉においては燃料を空気比0.3〜0.
8で燃焼させて鋼材を加熱し、前記第1のバッチ式加熱
炉で発生した燃焼ガスを第1のバッチ式加熱炉と第2の
バッチ式加熱炉を連結するダクトを経由して第2のバッ
チ式加熱炉に導入し、第2のバッチ式加熱炉では前記燃
焼ガスを空気比1.0以上で燃焼させて鋼材を加熱する
ことを特徴とするバッチ式加熱炉の操業方法。Claim 1: Using two batch-type heating furnaces, the first
In batch type heating furnaces, the fuel to air ratio is 0.3 to 0.
8 to heat the steel material, and the combustion gas generated in the first batch heating furnace is passed through a duct connecting the first batch heating furnace and the second batch heating furnace to the second batch heating furnace. A method for operating a batch-type heating furnace, characterized in that the steel material is heated by introducing the combustion gas into a batch-type heating furnace, and in a second batch-type heating furnace, the combustion gas is combusted at an air ratio of 1.0 or more.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3036467A JP2596235B2 (en) | 1991-03-04 | 1991-03-04 | Operating method of batch heating furnace |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3036467A JP2596235B2 (en) | 1991-03-04 | 1991-03-04 | Operating method of batch heating furnace |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH04276013A true JPH04276013A (en) | 1992-10-01 |
| JP2596235B2 JP2596235B2 (en) | 1997-04-02 |
Family
ID=12470619
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP3036467A Expired - Fee Related JP2596235B2 (en) | 1991-03-04 | 1991-03-04 | Operating method of batch heating furnace |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2596235B2 (en) |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5339848A (en) * | 1976-09-23 | 1978-04-12 | Siemens Ag | Method of indicating diffractive picture in transmission scanning particle beam microscope |
| JPH0257639A (en) * | 1988-08-22 | 1990-02-27 | Kobe Steel Ltd | Method for continuously heating steel strip |
-
1991
- 1991-03-04 JP JP3036467A patent/JP2596235B2/en not_active Expired - Fee Related
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5339848A (en) * | 1976-09-23 | 1978-04-12 | Siemens Ag | Method of indicating diffractive picture in transmission scanning particle beam microscope |
| JPH0257639A (en) * | 1988-08-22 | 1990-02-27 | Kobe Steel Ltd | Method for continuously heating steel strip |
Also Published As
| Publication number | Publication date |
|---|---|
| JP2596235B2 (en) | 1997-04-02 |
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