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JPH0144766B2 - - Google Patents
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JPH0144766B2 - - Google Patents

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Publication number
JPH0144766B2
JPH0144766B2 JP16595981A JP16595981A JPH0144766B2 JP H0144766 B2 JPH0144766 B2 JP H0144766B2 JP 16595981 A JP16595981 A JP 16595981A JP 16595981 A JP16595981 A JP 16595981A JP H0144766 B2 JPH0144766 B2 JP H0144766B2
Authority
JP
Japan
Prior art keywords
burners
combustion
state
burner
control stage
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.)
Expired
Application number
JP16595981A
Other languages
Japanese (ja)
Other versions
JPS5867820A (en
Inventor
Kenji Okamoto
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Sanken Sangyo Co Ltd
Original Assignee
Sanken Sangyo Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Sanken Sangyo Co Ltd filed Critical Sanken Sangyo Co Ltd
Priority to JP16595981A priority Critical patent/JPS5867820A/en
Priority to US06/426,374 priority patent/US4480992A/en
Priority to FR8217410A priority patent/FR2519739B1/en
Priority to GB08229720A priority patent/GB2113368B/en
Priority to DE19823238546 priority patent/DE3238546A1/en
Publication of JPS5867820A publication Critical patent/JPS5867820A/en
Publication of JPH0144766B2 publication Critical patent/JPH0144766B2/ja
Granted legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21DMODIFYING THE PHYSICAL STRUCTURE OF FERROUS METALS; GENERAL DEVICES FOR HEAT TREATMENT OF FERROUS OR NON-FERROUS METALS OR ALLOYS; MAKING METAL MALLEABLE, e.g. BY DECARBURISATION OR TEMPERING
    • C21D1/00General methods or devices for heat treatment, e.g. annealing, hardening, quenching or tempering
    • C21D1/34Methods of heating
    • C21D1/52Methods of heating with flames
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27DDETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
    • F27D19/00Arrangements of controlling devices
    • F27D2019/0006Monitoring the characteristics (composition, quantities, temperature, pressure) of at least one of the gases of the kiln atmosphere and using it as a controlling value
    • F27D2019/0018Monitoring the temperature of the atmosphere of the kiln
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27DDETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
    • F27D19/00Arrangements of controlling devices
    • F27D2019/0028Regulation
    • F27D2019/0034Regulation through control of a heating quantity such as fuel, oxidant or intensity of current

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Mechanical Engineering (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Heat Treatments In General, Especially Conveying And Cooling (AREA)
  • Control Of Heat Treatment Processes (AREA)

Description

【発明の詳細な説明】 この発明は鉄や鋼等の熱処理に使用するバツチ
炉を効率よく加熱すると共に、排ガス中の有害成
分を少なくしたバツチ炉の加熱法に関するもので
ある。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for heating batch furnaces used for heat treatment of iron, steel, etc., which efficiently heats batch furnaces and reduces harmful components in exhaust gas.

バツチ式の加熱炉の場合、加熱初期には燃焼量
が最大であり、大量の燃焼ガスが炉内を循環する
が、その後徐々に燃焼量は減少し、均熱加熱時に
は初期加熱時の1/10〜1/100の熱量しか必要とし
ない。この熱量減少方法として空気と燃料の両方
を絞る定空燃比燃焼システムが既に使用されてい
るが、燃焼量の減少とともに炉室内における空気
の循環が悪くなり温度の均一性保持に問題が生じ
る。また、空気を最大燃焼時の量で固定し、単に
燃料量のみを減じてゆく定空気燃焼システムも既
に使用されているが、僅かな熱量しか必要としな
い均熱加熱時に冷たい大量の余分な空気が入るた
め、炉室内における空気の循環はよいが燃焼効率
が悪い。更に、全部のバーナーを一斉にオン・オ
フするインパルス燃焼システムも既に使用されて
いるが、均熱加熱時におけるバーナーのオフ時間
が長く、且つこのオフ時間中炉内ガスの循環が全
く行われないので、炉内温度の均一化を図ること
が困難である。更にまた、特殊なノズルを使用
し、定空気燃焼システムと定空燃比燃焼システム
とを組合せた特殊なシステムも知られているが、
構造が複雑化し且つ低燃焼時における燃焼効率の
向上にいま一歩の感がある。この発明は、このよ
うな問題点を解決するためなされたものである。
In the case of batch-type heating furnaces, the amount of combustion is at its maximum at the beginning of heating, and a large amount of combustion gas circulates in the furnace, but after that, the amount of combustion gradually decreases, and during soaking heating, the amount of combustion is 1/1 of the initial heating. It requires only 10 to 1/100 the amount of heat. As a method for reducing the amount of heat, a constant air-fuel ratio combustion system that throttles both air and fuel has already been used, but as the amount of combustion decreases, air circulation within the furnace chamber deteriorates, causing problems in maintaining temperature uniformity. Also, constant air combustion systems are already in use, in which the amount of air is fixed at the maximum combustion level and only the amount of fuel is reduced. Although air circulation inside the furnace chamber is good, combustion efficiency is poor. Furthermore, impulse combustion systems that turn on and off all burners at the same time are already in use, but the burner off time during uniform heating is long, and during this off time there is no circulation of gas in the furnace. Therefore, it is difficult to equalize the temperature inside the furnace. Furthermore, a special system that uses a special nozzle and combines a constant air combustion system and a constant air fuel ratio combustion system is also known.
The structure is complicated and there is a feeling that there is still a way to improve combustion efficiency at low combustion times. This invention was made to solve these problems.

第1図乃至第8図に基いてこの発明の第1の実
施例を説明する。
A first embodiment of the present invention will be described based on FIGS. 1 to 8.

9はバツチ式加熱炉、10は加熱炉9の炉室、
1,2,3は第1図及び第2図において炉室10
の右側壁に設けた高速ジエツトバーナー、4,
5,6は同じく第1図及び第2図において炉室1
0の左側壁に設けた高速ジエツトバーナーで、加
熱炉9の炉長方向に沿つて左右のバーナーは順次
食違わせて配置されている。なお、これらのバー
ナーは、操作することにより着火後常にオン状態
で燃焼するところのオン維持バーナーとなる場合
と、着火後オン状態とオフ状態とが交互に行われ
るところのオン・オフ作動バーナーとなる場合と
があり、オン状態の燃焼中は最大の空気噴出量及
び最大の燃焼噴出量における定空燃比燃焼を行う
ようになつており、またオフ状態においては空気
も燃料もいずれも噴出しないようになつている。
この第1の実施例においては炉室10における燃
焼量をバーナーの着火本数を変えることによつて
段階的に制御するため次の5つの場合を設定す
る。すなわち、第1制御段においては、燃焼量が
一番少なく、一時にバーナーを1本だけ燃焼させ
るが複数本にわたつて順次切換えて点火するもの
である。これを第3図により説明すると、横軸に
時間をとり、縦軸に燃焼するバーナーの符号をと
り、最初の1単位Tの時間においてバーナー1を
点火燃焼させ、次の1単位の時間ではバーナー5
に切り換えて燃焼させる。このように、順次バー
ナーを1本ずつ燃焼し6つの単位時間を1周期L
として燃焼し、これが繰り返される。
9 is a batch type heating furnace, 10 is a furnace chamber of the heating furnace 9,
1, 2, and 3 are the furnace chambers 10 in FIGS. 1 and 2.
High-speed jet burner installed on the right side wall of 4.
5 and 6 are the furnace chamber 1 in Figures 1 and 2.
A high-speed jet burner is installed on the left side wall of the heating furnace 9, and the left and right burners are sequentially arranged at different intervals along the furnace length direction of the heating furnace 9. In addition, these burners can be operated as on-keeping burners, in which combustion is always on after ignition, or on/off operation burners, in which the on-state and off-state are alternately performed after ignition. During combustion in the on state, combustion is performed at a constant air-fuel ratio with the maximum air injection amount and maximum combustion ejection amount, and in the off state, neither air nor fuel is ejected. It's getting old.
In this first embodiment, the following five cases are set in order to control the combustion amount in the furnace chamber 10 in stages by changing the number of ignited burners. That is, in the first control stage, the combustion amount is the smallest, and only one burner is fired at a time, but multiple burners are sequentially switched and ignited. To explain this using Fig. 3, the horizontal axis represents time, and the vertical axis represents the sign of the burner being burned.In the first unit of time T, burner 1 is ignited and burned, and in the next unit of time, burner 1 is ignited and burned. 5
Switch to burn it. In this way, one burner is burned one by one, and one cycle L takes 6 units of time.
This process is repeated.

この第1制御段では各バーナーは全て自己の分
担時間中、オン・オフ作動バーナーとして作動
し、第8図のグラフでは点線で示してある。
In this first stage of control, each burner all operates as an on-off burner during its assigned time, as shown by the dotted line in the graph of FIG.

なお、オン・オフ作動バーナーはオンの時間を
短くし、オフの時間を長くすれば、バーナーフレ
ームの大きさは同一でも分担時間中における発熱
量は少くなり、またオンの時間を長くし、オフの
時間を短くすれば、分担時間中における発熱量は
多くなる。この第1制御段で0から最大発熱量の
1/6までの発熱を行う。
For on-off operation burners, if you shorten the on time and lengthen the off time, the amount of heat generated during the shared time will be lower even if the size of the burner frame is the same. If the time is shortened, the amount of heat generated during the shared time will increase. In this first control stage, heat is generated from 0 to 1/6 of the maximum heat generation amount.

次に、第2制御段においては、一時に2本のバ
ーナーを燃焼させる。これを第4図により説明す
ると、最初の1単位Tの時間ではバーナー1とバ
ーナー5とを点火燃焼する。この場合一方のバー
ナー1が実線で示すオン維持バーナーで、他方の
バーナー5は点線で示すオン・オフ作動バーナー
である。次の1単位の時間ではバーナー3とバー
ナー5とが点火燃焼し、このようにして順次バー
ナーが2本ずつ切換わり6つの単位時間を1周期
Lとして燃焼する。オン・オフ作動バーナーはこ
の場合もオンとオフの時間割合を変えることによ
り発熱量の調整が行われ、この第2制御段で、最
大発熱量の1/6〜2/6の発熱を行う。
Next, in the second control stage, two burners are fired at once. To explain this with reference to FIG. 4, during the first unit of time T, burners 1 and 5 are ignited and burned. In this case, one burner 1 is a keep-on burner, shown in solid lines, and the other burner 5 is an on-off operating burner, shown in dotted lines. In the next unit of time, burner 3 and burner 5 are ignited and burned, and in this way, the burners are sequentially switched two by two, and combustion is performed for six unit times as one cycle L. In this case as well, the on-off operating burner adjusts the amount of heat generated by changing the on/off time ratio, and in this second control stage, heat is generated between 1/6 and 2/6 of the maximum amount of heat.

第3制御段では第5図に示す如く単位Tの2倍
の時間が1周期Lとなり、各単位を2本のオン維
持バーナーと、1本のオン・オフ作動バーナーと
によつて発熱量の調整を行う。
In the third control stage, as shown in Fig. 5, one period L is twice the time of the unit T, and each unit is controlled by two on-keeping burners and one on/off operation burner to control the amount of heat generated. Make adjustments.

第4制御段では第6図に示す如く単位Tの2倍
の時間が1周期Lとなり、各単位を3本のオン維
持バーナーと、2本(ただし、いずれか1本のみ
がオンの状態にあり、2本が同時にオンとなるこ
とはない)のオン・オフ作動バーナーとによつて
発熱量の調整を行う。この第4制御段で、最大発
熱量の3/6〜4/6の発熱を行う。
In the fourth control stage, as shown in Fig. 6, one period L is twice the time of the unit T, and each unit is controlled by three on-keeping burners and two (however, only one burner is on). The amount of heat generated is adjusted by the on/off operation burners (both burners are not on at the same time). In this fourth control stage, 3/6 to 4/6 of the maximum heat generation amount is generated.

第5制御段では第7図に示す如く1単位Tの時
間が1周期Lとなり、各単位を4本のオン維持バ
ーナーと2本のオン・オフ作動バーナーとによつ
て発熱量の調整を行う。この第5制御段階で、最
大発熱量の4/6〜6/6の発熱を行う(なおこの制御
段は4/6〜5/6と5/6〜6/6の2つの段階に分けるこ
とが出来る)。
In the fifth control stage, as shown in Fig. 7, the time of one unit T becomes one period L, and the heat generation amount of each unit is adjusted by four on-keeping burners and two on-off operating burners. . In this fifth control stage, heat is generated from 4/6 to 6/6 of the maximum heat amount (this control stage is divided into two stages, 4/6 to 5/6 and 5/6 to 6/6). ).

第8図は制御段と燃焼量との関係を示すグラフ
で、横軸に制御段をまた縦軸に燃焼量をとつてい
る。1,2,3,4,5はそれぞれ制御段数を示
し、Aがオン・オフ作動バーナーによる燃焼部分
を表わし、Bがオン維持バーナーによる燃焼部分
を表わしている。
FIG. 8 is a graph showing the relationship between the control stage and the combustion amount, with the horizontal axis representing the control stage and the vertical axis representing the combustion amount. 1, 2, 3, 4, and 5 each indicate the number of control stages, A represents the combustion portion by the on-off operating burner, and B represents the combustion portion by the on-maintaining burner.

第9図乃至第17図に基いてこの発明の第2の
実施例を説明する。
A second embodiment of the present invention will be explained based on FIGS. 9 to 17.

この実施例のものにおいては、炉室10の左天
井バーナー17、右側壁バーナー11、左側壁バ
ーナー13、右天井バーナー15、左天井バーナ
ー18、右側壁バーナー12、左側壁バーナー1
4、右天井バーナー16が、炉室10の長手方向
に沿つて順次ずらせて配置されている。そして各
側壁バーナー11,12,13,14は各天井バ
ーナー15,16,17,18の能力の1/2の出
力に設定されている。
In this embodiment, the left ceiling burner 17, the right side wall burner 11, the left side wall burner 13, the right ceiling burner 15, the left ceiling burner 18, the right side wall burner 12, and the left side wall burner 1 of the furnace chamber 10.
4. The right ceiling burners 16 are arranged to be sequentially shifted along the longitudinal direction of the furnace chamber 10. Each of the side wall burners 11, 12, 13, and 14 is set to output half the capacity of each of the ceiling burners 15, 16, 17, and 18.

また、各側壁バーナー11,12,13,14
はオン維持状態とオン・オフ作動状態のいずれで
も行える。しかし天井バーナー15,16,1
7,18はオン維持状態のみで行え、オン・オフ
作動状態は行えない。
In addition, each side wall burner 11, 12, 13, 14
can be performed in either the on-maintenance state or the on-off operating state. But ceiling burners 15, 16, 1
7 and 18 can be performed only in the ON maintenance state, and cannot be performed in the ON/OFF operation state.

第11図は第1制御段状態を示すグラフで、単
位Tの4倍が1周期Lとなり、各単位を4本の側
壁バーナーが順次1本ずつオン・オフ作動バーナ
ーとして発熱量の調整を行う。この第1制御段
で、最大発熱量の0〜1/12の発熱を行う。
Figure 11 is a graph showing the state of the first control stage, where 4 times the unit T is one period L, and each unit has four side wall burners that adjust the heat output one by one as an on/off burner. . In this first control stage, heat is generated between 0 and 1/12 of the maximum heat amount.

第12図は第2制御段状態を示すグラフで、単
位Tの6倍が1周期Lとなり、4本の側壁バーナ
ーが各単位を1本のオン維持側壁バーナーと1本
のオン・オフ作動側壁バーナーとによつて発熱量
の調整を行う。この第2制御段で最大発熱量の1/
12〜2/12の発熱を行う。
Figure 12 is a graph showing the state of the second control stage, where 6 times the unit T is one period L, and each unit has four sidewall burners, one on-keeping sidewall burner, and one on/off operation sidewall. The amount of heat generated is adjusted by the burner. This second control stage produces 1/1 of the maximum heat generation amount.
12 to 2/12 fever.

第13図は第3制御段状態を示すグラフで、単
位Tの2倍が1周期Lとなり、4本の側壁バーナ
ーが各単位をそれぞれ2本のオン維持側壁バーナ
ーと2本のオン・オフ作動側壁バーナーとによつ
て発熱量の調整を行う。この第3制御段で、最大
発熱量の2/12〜4/12の発熱を行う。
Figure 13 is a graph showing the state of the third control stage, where twice the unit T is one period L, and four side wall burners maintain each unit with two side wall burners on and two on/off operations. The amount of heat generated is adjusted by the side wall burner. In this third control stage, heat is generated from 2/12 to 4/12 of the maximum heat amount.

第14図は第4制御段状態を示すグラフで、単
位Tの2倍が1周期Lとなり、2本のオン・オフ
作動側壁バーナーと2本のオン維持天井バーナー
とによつて発熱量の調整を行う。この第4制御段
で、最大発熱量の4/12〜6/12の発熱を行う。
Figure 14 is a graph showing the state of the fourth control stage, where twice the unit T is one cycle L, and the amount of heat generated is adjusted by two on-off operating side wall burners and two on-maintaining ceiling burners. I do. In this fourth control stage, heat is generated from 4/12 to 6/12 of the maximum heat amount.

第15図は第5制御段状態を示すグラフで、単
位Tの2倍が1周期Lとなり、各単位をそれぞれ
2本のオン維持側壁バーナー、2本のオン・オフ
作動側壁バーナー、2本のオン維持天井バーナー
とによつて発熱量の調整を行う。この第5制御段
で、最大発熱量の6/12〜8/12の発熱を行う。
FIG. 15 is a graph showing the state of the fifth control stage, where twice the unit T is one period L, and each unit is divided into two on-keeping side wall burners, two on/off operation side wall burners, and two on-off operation side wall burners. The amount of heat generated is adjusted by keeping the ceiling burner on. In this fifth control stage, heat is generated from 6/12 to 8/12 of the maximum heat amount.

第16図は第6制御段状態を示すグラフで、4
本のオン・オフ作動側壁バーナーと4本のオン維
持天井バーナーとによつて発熱量の調整を行う。
この第6制御段で、最大発熱量の8/12〜12/12の
発熱を行う。
FIG. 16 is a graph showing the state of the sixth control stage.
The amount of heat generated is regulated by a book on/off side wall burner and four on/off ceiling burners.
In this sixth control stage, heat of 8/12 to 12/12 of the maximum heat amount is generated.

第17図は、第1実施例の第8図相当図で、A
の部分がオン・オフ作動側壁バーナー、Bの部分
がオン維持側壁バーナー、Cの部分がオン維持天
井バーナーによる燃焼部分を表している。
FIG. 17 is a diagram corresponding to FIG. 8 of the first embodiment, and A
The part B represents the side wall burner that operates on and off, the part B represents the side wall burner that remains on, and the part C represents the combustion part that uses the ceiling burner that maintains on.

上述した如くこの発明に係るバツチ炉の加熱法
は、着火後の単位時間T中は燃焼のみするところ
のオン維持状態と、着火後の単位時間T中は短時
間間隔で燃焼状態と非燃焼状態とを交互に行うと
ころのオン・オフ作動状態とが行え且つ着火中は
燃焼効率のよい定空燃比で而も全負荷運転する偶
数個の高速ジエツトバーナーを、炉長方向に沿つ
て炉室の左右両側壁に食違わせた状態で交互に開
口させ、 且つ同一制御段においては炉室の左半分と右半
分とが、同一本数のオン維持状態のバーナー及び
同一本数のオン・オフ作動状態のバーナーを単位
時間T毎に交互に有し、 而もオン維持状態のバーナー及びオン・オフ作
動状態のバーナーは、炉室の炉長方向に沿つて炉
室の左半分と右半分とから交互に位置を占めて燃
焼すると共に、 単位時間の任意倍数を周期Lとして同一燃焼順
序を繰返し、 而も燃焼制御段の増加と共にオン維持状態のバ
ーナーが増え、また燃焼量最小の第1制御段を除
き、単位時間T内におけるオン維持状態のバーナ
ー本数がオン・オフ作動状態のバーナー本数以上
になるようにしたものである。
As described above, the heating method of the batch furnace according to the present invention has two states: a continuous ON state in which only combustion occurs during the unit time T after ignition, and a combustion state and a non-combustion state at short intervals during the unit time T after ignition. An even number of high-speed jet burners are installed in the furnace chamber along the length of the furnace. The left and right side walls of the furnace chamber are opened alternately in a staggered manner, and in the same control stage, the left and right halves of the furnace chamber have the same number of burners kept on and the same number of burners in on/off operation. The burners are arranged alternately every unit time T, and the burners in the ON state and the burners in the ON/OFF state are alternately arranged from the left half and the right half of the furnace chamber along the length direction of the furnace chamber. At the same time, the same combustion order is repeated with the period L being an arbitrary multiple of the unit time, and as the number of combustion control stages increases, the number of burners kept on increases, and the first control stage with the minimum combustion amount is Except for this, the number of burners kept on within a unit time T is greater than the number of burners kept on/off.

それでは、全燃焼範囲に亙つて燃焼効率の最も
高い空燃比で燃焼を行い、且つ使用バーナーが高
速ジエツトバーナーなので大量の伴流ガスが炉内
を撹拌し昇温・均熱期を通じて温度の均一化を確
保することが出来る。
Now, combustion is performed at the air-fuel ratio with the highest combustion efficiency over the entire combustion range, and since the burner used is a high-speed jet burner, a large amount of wake gas is stirred inside the furnace and the temperature is uniform throughout the heating and soaking periods. It is possible to ensure that

また、同一制御段においては、炉室の左半分と
右半分とが、同一本数のオン維持状態のバーナー
及びオン・オフ作動状態のバーナーを、単位時間
T毎に交互に位置換えするので、炉室の左半分と
右半分との加熱量が等しくなつて斑加熱が生じる
のが防げる。
In addition, in the same control stage, the left half and right half of the furnace chamber have the same number of burners kept on and burners in the on/off operation state, which are alternately repositioned every unit time T. The amount of heating in the left and right halves of the chamber becomes equal, preventing uneven heating from occurring.

更に単位時間Tの任意倍数を周期Lとし、同一
の燃焼順序を繰返えすので、設計・制御も容易の
なり炉室内の循環空気流は炉長方向に沿つて次々
と逆転するので、被処理物に対して熱効率の良い
加熱をすることが出来る。
Furthermore, since the period L is an arbitrary multiple of the unit time T, and the same combustion order is repeated, design and control are easy. It is possible to heat objects with high thermal efficiency.

更にまた燃焼量最小の第1制御段を除きオン維
持状態のバーナー本数がオン・オフ作動状態のバ
ーナー本数以上あるので、炉室内温度の斑発生を
極めて少なくすることが出来る。そのうえ、第1
制御段を除きいずれの制御段においても、炉室左
側からの作動中にバーナー及び右側からの作動中
のバーナーが炉長方向に沿つて交互に配置されて
いるので、斑の少ない加熱を行うことが出来る。
Furthermore, since the number of burners kept in the ON state is greater than the number of burners in the ON/OFF operation state, except for the first control stage with the minimum combustion amount, it is possible to extremely reduce the occurrence of temperature irregularities in the furnace interior. Moreover, the first
In all control stages except the control stage, the burners operating from the left side of the furnace chamber and the burners operating from the right side are alternately arranged along the furnace length direction, so heating can be performed with less unevenness. I can do it.

それ故、局処過熱もなく、全範囲に亙つて省エ
ネルギー操業及び低公害(特にNOxの発生が少
ない)操業が可能である。
Therefore, there is no localized overheating, and energy-saving and low-pollution (particularly low NOx generation) operation is possible over the entire range.

【図面の簡単な説明】[Brief explanation of drawings]

第1図乃至第8図はこの発明に係るバツチ炉の
加熱法の第1の実施例を説明するためのもので、
第1図はバツチ式加熱炉の概略正面図、第2図は
同上平面図、第3図は第1制御段の作動状態を示
すグラフ、第4図は第2制御段の作動状態を示す
グラフ、第5図は第3制御段の作動状態を示すグ
ラフ、第6図は第4制御段の作動状態を示すグラ
フ、第7図は第5制御段の作動状態を示すグラ
フ、第8図は制御段と燃焼量との関係を示すグラ
フである。第9図乃至第17図はこの発明に係る
炉の加熱法の第2の実施例を説明するためのもの
で、第9図はバツチ式加熱炉の概略正面図、第1
0図は同上平面図、第11図は第1制御段の作動
状態を示すグラフ、第12図は第2制御段の作動
状態を示すグラフ、第13図は第3制御段の作動
状態を示すグラフ、第14図は第4制御段の作動
状態を示すグラフ、第15図は第5制御段の作動
状態を示すグラフ、第16図は第6制御段の作動
状態を示すグラフ、第17図は制御段と燃焼量と
の関係を示すグラフである。 1……バーナー、2……バーナー、3……バー
ナー、4……バーナー、5……バーナー、6……
バーナー、9……バツチ式加熱炉、10……炉
室、11……バーナー、12……バーナー、13
……バーナー、14……バーナー、15……バー
ナー、16……バーナー、17……バーナー、1
8……バーナー。
1 to 8 are for explaining a first embodiment of the batch furnace heating method according to the present invention,
Fig. 1 is a schematic front view of the batch heating furnace, Fig. 2 is a plan view of the same as above, Fig. 3 is a graph showing the operating state of the first control stage, and Fig. 4 is a graph showing the operating state of the second control stage. , Fig. 5 is a graph showing the operating state of the third control stage, Fig. 6 is a graph showing the operating state of the fourth control stage, Fig. 7 is a graph showing the operating state of the fifth control stage, and Fig. 8 is a graph showing the operating state of the fifth control stage. It is a graph showing the relationship between control stage and combustion amount. 9 to 17 are for explaining a second embodiment of the furnace heating method according to the present invention, and FIG. 9 is a schematic front view of a batch-type heating furnace;
Figure 0 is a plan view of the same as above, Figure 11 is a graph showing the operating state of the first control stage, Figure 12 is a graph showing the operating state of the second control stage, and Figure 13 is a graph showing the operating state of the third control stage. Graph, FIG. 14 is a graph showing the operating state of the fourth control stage, FIG. 15 is a graph showing the operating state of the fifth control stage, FIG. 16 is a graph showing the operating state of the sixth control stage, and FIG. 17 is a graph showing the operating state of the sixth control stage. is a graph showing the relationship between the control stage and the combustion amount. 1... Burner, 2... Burner, 3... Burner, 4... Burner, 5... Burner, 6...
Burner, 9... Batch type heating furnace, 10... Furnace chamber, 11... Burner, 12... Burner, 13
... Burner, 14 ... Burner, 15 ... Burner, 16 ... Burner, 17 ... Burner, 1
8...Burner.

Claims (1)

【特許請求の範囲】 1 着火後の単位時間(T)中は燃焼のみすると
ころのオン維持状態と、着火後の単位時間(T)
中は短時間間隔で燃焼状態と非燃焼状態とを交互
に行うところのオン・オフ作動状態とが行え且つ
着火中は燃焼効率のよい定空燃比で而も全負荷運
転する偶数個の高速ジエツトバーナーを、炉長方
向に沿つて炉室の左右両側壁に食違わせた状態で
交互に開口させ、 且つ同一制御段においては炉室の左半分と右半
分とが、同一本数のオン維持状態のバーナー及び
同一本数のオン・オフ作動状態のバーナーを単位
時間(T)毎に交互に有し、 而もオン維持状態のバーナー及びオン・オフ作
動状態のバーナーは、炉室の炉長方向に沿つて炉
室の左半分と右半分とから交互に位置を占めて燃
焼すると共に、 単位時間(T)の任意倍数を周期(L)として同一
燃焼順序を繰返し、 而も燃焼制御段の増加と共にオン維持状態のバ
ーナーが増え、また燃焼量最小の第1制御段を除
き、単位時間(T)内におけるオン維持状態のバ
ーナー本数がオン・オフ作動状態のバーナー本数
以上あることを特徴とするバツチ炉の加熱法。
[Claims] 1. On-maintenance state in which only combustion occurs during the unit time (T) after ignition, and the unit time (T) after ignition
During ignition, an even number of high-speed engines are operated at a constant air-fuel ratio with good combustion efficiency, and at full load. The exhaust burners are opened alternately along the furnace length direction on the left and right side walls of the furnace chamber, and in the same control stage, the same number of burners are kept turned on in the left and right halves of the furnace chamber. The burners in the ON state and the same number of burners in the ON/OFF operating state are arranged alternately every unit time (T), and the burners in the ON state and the burners in the ON/OFF operating state are arranged in the furnace length direction of the furnace chamber. , the combustion takes place alternately from the left half and the right half of the furnace chamber, and the same combustion order is repeated with the period (L) being an arbitrary multiple of the unit time (T), and the number of combustion control stages increases. At the same time, the number of burners in the ON state increases, and the number of burners in the ON state within a unit time (T) is greater than the number of burners in the ON/OFF operating state, except for the first control stage with the minimum combustion amount. Batch furnace heating method.
JP16595981A 1981-10-17 1981-10-17 Method for heating furnace Granted JPS5867820A (en)

Priority Applications (5)

Application Number Priority Date Filing Date Title
JP16595981A JPS5867820A (en) 1981-10-17 1981-10-17 Method for heating furnace
US06/426,374 US4480992A (en) 1981-10-17 1982-09-29 Method of heating a furnace
FR8217410A FR2519739B1 (en) 1981-10-17 1982-10-18 METHOD FOR HEATING A HEAT TREATMENT OVEN
GB08229720A GB2113368B (en) 1981-10-17 1982-10-18 Method of heating a furnace
DE19823238546 DE3238546A1 (en) 1981-10-17 1982-10-18 METHOD FOR HEATING A STOVE

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16595981A JPS5867820A (en) 1981-10-17 1981-10-17 Method for heating furnace

Related Child Applications (1)

Application Number Title Priority Date Filing Date
JP5979486A Division JPS61264127A (en) 1986-03-17 1986-03-17 Heater for furnace

Publications (2)

Publication Number Publication Date
JPS5867820A JPS5867820A (en) 1983-04-22
JPH0144766B2 true JPH0144766B2 (en) 1989-09-29

Family

ID=15822261

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16595981A Granted JPS5867820A (en) 1981-10-17 1981-10-17 Method for heating furnace

Country Status (1)

Country Link
JP (1) JPS5867820A (en)

Also Published As

Publication number Publication date
JPS5867820A (en) 1983-04-22

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