JPH0816529B2 - Furnace temperature control method - Google Patents
Furnace temperature control methodInfo
- Publication number
- JPH0816529B2 JPH0816529B2 JP3050210A JP5021091A JPH0816529B2 JP H0816529 B2 JPH0816529 B2 JP H0816529B2 JP 3050210 A JP3050210 A JP 3050210A JP 5021091 A JP5021091 A JP 5021091A JP H0816529 B2 JPH0816529 B2 JP H0816529B2
- Authority
- JP
- Japan
- Prior art keywords
- furnace
- combustion
- burner
- heat storage
- combustion gas
- 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 - Fee Related
Links
- 238000000034 method Methods 0.000 title description 9
- 238000002485 combustion reaction Methods 0.000 claims description 35
- 239000000567 combustion gas Substances 0.000 claims description 31
- 238000005338 heat storage Methods 0.000 claims description 26
- 238000007599 discharging Methods 0.000 claims description 7
- 238000010438 heat treatment Methods 0.000 claims description 6
- 239000000446 fuel Substances 0.000 description 12
- 239000007789 gas Substances 0.000 description 6
- 230000006698 induction Effects 0.000 description 5
- 230000007423 decrease Effects 0.000 description 4
- 238000011084 recovery Methods 0.000 description 4
- 239000011819 refractory material Substances 0.000 description 2
- 230000001172 regenerating effect Effects 0.000 description 2
- 230000002411 adverse Effects 0.000 description 1
- 239000011449 brick Substances 0.000 description 1
- 238000009841 combustion method Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 238000003303 reheating Methods 0.000 description 1
- 230000004043 responsiveness Effects 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/34—Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery
Landscapes
- Air Supply (AREA)
- Regulation And Control Of Combustion (AREA)
- Gas Burners (AREA)
Description
【発明の詳細な説明】Detailed Description of the Invention
【0001】[0001]
【産業上の利用分野】本発明は炉温制御方法に関する。
更に詳述すると、本発明は迅速な炉温調整が可能な炉温
制御方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a furnace temperature control method.
More specifically, the present invention relates to a furnace temperature control method capable of rapid furnace temperature adjustment.
【0002】[0002]
【従来の技術】従来の加熱炉における炉温調整手段とし
てはバーナの燃焼量を変えることが最も一般的である。
また、付加的な炉温調整手段としては空気比を調整する
ことが一般的である。2. Description of the Related Art As a furnace temperature adjusting means in a conventional heating furnace, changing the combustion amount of a burner is the most common.
Further, as an additional furnace temperature adjusting means, it is general to adjust the air ratio.
【0003】[0003]
【発明が解決しようとする課題】しかしながら、燃焼量
を調節することは最も確実に炉温調整が可能であるが、
焼却炉(インシネレータ)のように燃焼させること即ち
焼却そのものを目的としている炉の場合、燃焼量調節は
即ち処理量調節となり全量処理が必要なインシネレータ
の場合には極めて不都合である。また、一般の加熱炉に
おいて燃焼量を調節することによって炉温調整を行なう
場合、これを急激に行うと、失火や空気比の狂いを招く
ことから、どうしても徐々に変化させることしかできず
応答性が悪い。また、低カロリーガスのように自燃し得
ない燃料を燃焼させるための追い焚きにおいても燃焼量
を調節することは燃焼そのものを不安定にする虞があ
る。更に、燃焼量の調整を行うと一般に火炎長が変化す
るため炉内の伝熱機構が変化し炉内を均一に加熱するこ
とに悪影響を及ぼす場合がほとんどである。However, although the combustion temperature can be adjusted most reliably by adjusting the combustion amount,
In the case of a furnace whose purpose is to combust like an incinerator (incinerator), that is, incineration itself, the adjustment of the combustion amount is an adjustment of the treatment amount, which is extremely inconvenient in the case of an incinerator that requires a total treatment. Also, in the case of adjusting the furnace temperature by adjusting the combustion amount in a general heating furnace, if this is suddenly performed, misfire or an air ratio error will occur, so it can only be gradually changed and the responsiveness Is bad. In addition, even in reheating for burning a fuel that cannot self-combust, such as low-calorie gas, adjusting the combustion amount may make combustion itself unstable. Furthermore, when the amount of combustion is adjusted, the flame length generally changes, so the heat transfer mechanism in the furnace changes, and in most cases adversely affects uniform heating in the furnace.
【0004】また、空気比を変化させる場合、バーナの
安定燃焼範囲を越えて炉温を調節することが不可能であ
る。しかも、一般に最も安定燃焼する空気比範囲はかな
り狭いことから調節範囲は相当狭められる。When changing the air ratio, it is impossible to control the furnace temperature beyond the stable combustion range of the burner. In addition, since the air ratio range in which the most stable combustion is performed is generally narrow, the adjustment range is considerably narrowed.
【0005】本発明は燃焼量を制御することなく炉温調
節が確実かつ素早く応答できる炉温制御方法を提供する
ことを目的とする。It is an object of the present invention to provide a furnace temperature control method capable of reliably and quickly responding to the furnace temperature control without controlling the combustion amount.
【0006】[0006]
【課題を解決するための手段】かかる目的を達成するた
め、本発明の炉温制御方法は、バーナを熱源とする加熱
炉において、蓄熱体を備えると共に該蓄熱体を通して燃
焼用空気の供給及び燃焼ガスの排出を行なう蓄熱型バー
ナを少なくとも1組炉体に設置し、これらバーナを交互
に燃焼させて燃焼させていない方のバーナから前記蓄熱
体を経て燃焼ガスを排出させる第1の排気手段と、前記
燃焼ガスを前記バーナを通さずに炉外へ排出する第2の
排気手段とを設け、この第2の排気手段を操作すること
によって前記バーナを通過する燃焼ガスの量を変化させ
て炉温を制御するようにしている。In order to achieve such an object, the furnace temperature control method of the present invention is a heating furnace using a burner as a heat source, which is provided with a regenerator and supplies and burns combustion air through the regenerator. A first exhaust means for installing a heat storage type burner for discharging gas in at least one assembled furnace body, and for alternately burning these burners to discharge combustion gas from the burner which has not been burned through the heat storage body; Second exhaust means for discharging the combustion gas to the outside of the furnace without passing through the burner, and by operating the second exhaust means, the amount of the combustion gas passing through the burner is changed. I try to control the temperature.
【0007】[0007]
【作用】したがって、炉温調節が必要な場合、第2の排
気手段を操作して直接炉外に排出される燃焼ガス量を変
えることによって蓄熱型バーナの蓄熱体へ供給される燃
焼ガス量を変化させる。これにより、燃焼用空気の予熱
温度を変化させ、燃焼量とは無関係に火炎温度を変化さ
せる。Therefore, when it is necessary to adjust the furnace temperature, the second exhaust means is operated to directly change the amount of the combustion gas discharged to the outside of the furnace, thereby changing the amount of the combustion gas supplied to the heat storage body of the heat storage type burner. Change. As a result, the preheating temperature of the combustion air is changed, and the flame temperature is changed regardless of the amount of combustion.
【0008】[0008]
【実施例】以下、本発明の構成を図面に示す実施例に基
づいて詳細に説明する。尚、この実施例はオープンフレ
ームバーナに適用したものである。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The structure of the present invention will be described in detail below with reference to the embodiments shown in the drawings. This embodiment is applied to an open frame burner.
【0009】図1に本発明の炉温制御方法を蓄熱型加熱
炉に実施した場合の炉構造の一実施例を示す。この炉
は、炉体1に少なくとも1組の蓄熱型バーナ2,3を設
置して成る。蓄熱型バーナ2,3は、その構造及び燃焼
方式に特に限定を受けるものではないが、本実施例にお
いては、ウィンドボックス4に燃焼用空気を供給する燃
焼用空気供給系7と燃焼ガスを排出する燃焼ガス排気系
8とを選択的に接続可能とし、蓄熱体5を通して燃焼用
空気の供給及び燃焼ガスの排出を図るように設けられて
いる。ウィンドボックス2の炉体1寄りのバーナスロー
ト部分には燃料を噴射する燃料ノズル6,6が埋設され
ている。この燃料ノズル6,6はバーナスロートを形成
する耐火物の内周面から燃料を噴射するように設けられ
ており、バーナスロート内を流れる燃焼用空気の流れに
対して燃料が交差するように設置されている。燃料ノズ
ル6,6は少なくとも1本埋設されておれば足りるが、
2本以上を円周方向に等間隔をあけて配置することによ
ってバーナスロートにおける占有面積割合を調整可能に
して燃料と空気の混合特性を変え得るようにし、かつバ
ーナスロートの中央において火炎が形成されるように設
けられている。また、燃料ノズル6,6から噴射される
燃料の流れと空気流との成す角度を変更することによっ
て燃料と空気の混合速度を変えて火炎長さを変化させ得
る。FIG. 1 shows an embodiment of the furnace structure when the furnace temperature control method of the present invention is applied to a heat storage type heating furnace. In this furnace, a furnace body 1 is provided with at least one set of regenerative burners 2 and 3. The heat storage type burners 2 and 3 are not particularly limited in their structure and combustion method, but in the present embodiment, the combustion air supply system 7 for supplying combustion air to the wind box 4 and the combustion gas are discharged. The combustion gas exhaust system 8 is selectively connectable to the combustion gas exhaust system 8 and is provided so as to supply combustion air and discharge combustion gas through the heat storage body 5. Fuel nozzles 6 and 6 for injecting fuel are embedded in a burner throat portion of the wind box 2 near the furnace body 1. The fuel nozzles 6 and 6 are provided so as to inject fuel from the inner peripheral surface of the refractory material forming the burner throat, and are installed so that the fuel intersects the flow of combustion air flowing in the burner throat. Has been done. It is sufficient if at least one fuel nozzle 6, 6 is buried,
By arranging two or more pieces at equal intervals in the circumferential direction, the occupied area ratio in the burner throat can be adjusted to change the mixing characteristics of fuel and air, and a flame is formed in the center of the burner throat. Is provided. Further, the flame length can be changed by changing the mixing speed of the fuel and air by changing the angle formed by the flow of the fuel injected from the fuel nozzles 6 and 6 and the air flow.
【0010】また、燃焼ガス排気系8と燃焼用空気供給
系7とは四方弁11によって選択的にいずれか一方のバ
ーナ2,3のウィンドボックス4に接続され、例えば押
し込みファン9によって供給される燃焼用空気がウイン
ドボックス4に供給されると同時に例えば誘引ファン1
0によって燃焼ガスがウインドボックス4から吸引され
大気中に排出される。また、燃料は三方弁13を介して
いずれか一方のバーナ2,3に選択的に供給される。
尚、燃焼ガス排気系8と誘引ファン10によって第1の
排気手段が構成されている。The combustion gas exhaust system 8 and the combustion air supply system 7 are selectively connected by a four-way valve 11 to the wind box 4 of one of the burners 2 and 3, and are supplied by, for example, a pushing fan 9. At the same time that the combustion air is supplied to the wind box 4, for example, the induction fan 1
By 0, combustion gas is sucked from the wind box 4 and discharged into the atmosphere. Further, the fuel is selectively supplied to either one of the burners 2 and 3 via the three-way valve 13.
The combustion gas exhaust system 8 and the induction fan 10 form a first exhaust means.
【0011】炉体1は通常耐火物例えば耐火レンガ等に
よって形成され、被加熱物の搬入・搬出口(図示省略)
の他に第2の排気手段16が設けられている。この第2
の排気手段16としては例えば開閉ダンパ15を有する
ダクト14が採用されている。このダクト14には必要
に応じて誘引ファン(図示省略)が設けられて誘引排気
が行われたり、あるいは煙突が接続されてトンネル効果
によって排気するように設けられている。本実施例の第
2の排気手段16はダンパ15の操作によってその開度
を変化させ排気量を調整可能としている。The furnace body 1 is usually made of a refractory material such as refractory bricks, and carries in / out a heated object (not shown).
In addition to the above, a second exhaust means 16 is provided. This second
As the exhaust means 16, the duct 14 having the opening / closing damper 15 is adopted. If necessary, an induction fan (not shown) is provided in the duct 14 to perform induction exhaust, or a chimney is connected to the duct 14 to provide exhaust by a tunnel effect. The second exhaust means 16 of the present embodiment can change the opening degree by operating the damper 15 to adjust the exhaust amount.
【0012】以上のように構成されているので、一対の
蓄熱型バーナ2,3を交互に燃焼させ、その燃焼ガスを
燃焼させていないバーナの燃焼ガス排気系8即ち第1の
排気手段を介して排気し、蓄熱体5に燃焼ガスの排熱を
回収する。したがって、炉内温度は燃焼量が一定の場合
には燃焼用空気の予熱温度に左右される。そこで、例え
ば炉内温度が炉壁や煙突等が焼損する虞が生ずる程に高
くなった場合、第2の排気手段16たるダクト14を開
いて炉1内の燃焼ガスを第2の排気手段16から排気
し、第1の排気手段の蓄熱体5を通して排気される燃焼
ガス量を少なくする。これによって、燃焼が切替えられ
た際、蓄熱体5を通して供給される燃焼用空気の温度が
下がるため燃焼量が一定であったとしても火炎温度は低
下する。更に、この低下した燃焼ガスの一部が反対側の
バーナの蓄熱体5を通して第1の排気手段から排出され
るため更に燃焼が切替えられた場合、火炎温度は更に低
くなる。依って、炉内温度は急激に低下する。With the above-mentioned structure, the pair of regenerative burners 2 and 3 are alternately burned, and the burned gas exhaust system 8 of the burner which does not burn the burned gas, that is, the first exhaust means. The exhaust heat of the combustion gas is recovered in the heat storage body 5. Therefore, the temperature in the furnace depends on the preheating temperature of the combustion air when the amount of combustion is constant. Therefore, for example, when the temperature inside the furnace becomes so high that the furnace wall, the chimney, etc. may be burned out, the duct 14 serving as the second exhaust means 16 is opened to remove the combustion gas in the furnace 1 from the second exhaust means 16. The amount of combustion gas discharged from the heat storage body 5 of the first exhaust means is reduced. As a result, when the combustion is switched, the temperature of the combustion air supplied through the heat storage body 5 decreases, so that the flame temperature decreases even if the combustion amount is constant. Further, when the combustion is further switched because a part of the lowered combustion gas is discharged from the first exhaust means through the heat storage body 5 of the burner on the opposite side, the flame temperature becomes further lower. Therefore, the temperature inside the furnace drops sharply.
【0013】この関係は、図2に示す熱風温度と排ガス
回収率との関係から明らかである。この図は説明の関連
のため放熱が0で燃焼ガスと蓄熱体5との間における熱
交換率が100%であると仮定した場合における燃焼用
空気予熱温度と燃焼ガス顕熱回収割合を示すもので、回
収率が下がる程に燃焼ガス温度が低下していくことが理
解できる。This relationship is clear from the relationship between the hot air temperature and the exhaust gas recovery rate shown in FIG. This figure shows the combustion air preheating temperature and the combustion gas sensible heat recovery rate when it is assumed that the heat radiation is 0 and the heat exchange rate between the combustion gas and the heat storage body 5 is 100% for the sake of explanation. Thus, it can be understood that the combustion gas temperature decreases as the recovery rate decreases.
【0014】尚、上述の実施例は本発明の好適な実施の
一例ではあるがこれに限定されるものではなく本発明の
要旨を逸脱しない範囲において種々変形実施可能であ
る。例えば、本実施例においてはオープンフレームバー
ナについて適用した実施例を説明したが、特にこれに限
定されるものではなくラジアントチューブバーナに適用
することも可能である。例えば、図示していないが蓄熱
体の前後を開通する開閉可能なバイパス路を設け、この
バイパス路の開閉によって燃焼ガスを蓄熱体を迂回して
排出するような第2の排気手段を構成すれば良い。この
場合、前述のバイパス路の開度を調節することによって
蓄熱体を通過せずにバイパスを通過して排出される燃焼
ガス量をコントロールすることができる。It should be noted that the above-mentioned embodiment is an example of a preferred embodiment of the present invention, but the present invention is not limited to this, and various modifications can be made without departing from the gist of the present invention. For example, although an example in which the present invention is applied to the open frame burner has been described, the present invention is not particularly limited to this, and the present invention can be applied to a radiant tube burner. For example, although not shown, if a bypass path that opens and closes the heat storage body is provided and that can be opened and closed, and if the second exhaust means is configured to discharge the combustion gas by bypassing the heat storage body by opening and closing the bypass path, good. In this case, the amount of combustion gas discharged through the bypass without passing through the heat storage body can be controlled by adjusting the opening degree of the bypass passage.
【0015】[0015]
【発明の効果】以上の説明より明らかなように、本発明
の炉温制御方法は、蓄熱体を通して燃焼用空気の供給及
び燃焼ガスの排出を行なう蓄熱型バーナを少なくとも1
組炉体に設置し、これらバーナを交互に燃焼させて燃焼
させていない方のバーナから蓄熱体を通して燃焼ガスを
排出させる第1の排気手段と、燃焼ガスをバーナを通さ
ずに炉外へ排出する第2の排気手段とを設け、この第2
の排気手段を操作することによってバーナを通過する燃
焼ガスの量を変化させることによって炉温を制御すよう
にしたので、燃焼量は一定のまま炉内温度を急速に変化
させることができる。しかも、本発明の炉温制御方法
は、燃焼量が一定のままで炉温調整ができるので、イン
シネレータや低カロリーガス燃焼装置のような燃焼その
ものを目的としている炉に実施する場合、燃焼量を変更
せずに連続燃焼させながら炉温だけを調整することがで
きる。As is apparent from the above description, the furnace temperature control method of the present invention includes at least one heat storage burner for supplying combustion air and discharging combustion gas through the heat storage body.
Installed in the assembled furnace body, the first exhaust means for alternately burning these burners and discharging the combustion gas from the burner that is not burning through the heat storage body, and discharging the combustion gas outside the furnace without passing through the burners. And a second exhaust means for
Since the furnace temperature is controlled by changing the amount of the combustion gas that passes through the burner by operating the exhaust means, the temperature inside the furnace can be rapidly changed while the combustion amount is constant. Moreover, since the furnace temperature control method of the present invention allows the furnace temperature to be adjusted while the combustion amount remains constant, when the furnace is intended for combustion itself such as an incinerator or a low-calorie gas combustion device, the combustion amount can be adjusted. Only the furnace temperature can be adjusted while continuously burning without changing.
【図1】本発明の炉温制御方法を実施する炉の一実施例
を示す断面図である。FIG. 1 is a sectional view showing an embodiment of a furnace for carrying out a furnace temperature control method of the present invention.
【図2】同バーナにおける燃焼用空気の温度と燃焼ガス
回収率との関係を示すグラフである。FIG. 2 is a graph showing a relationship between a temperature of combustion air and a combustion gas recovery rate in the burner.
1 炉体 2 蓄熱型バーナ 3 蓄熱型バーナ 5 蓄熱体 8 第1の排気手段を構成する燃焼ガス排気系 10 第1の排気手段を構成する誘引ファン 16 第2の排気手段 DESCRIPTION OF SYMBOLS 1 Furnace body 2 Heat storage type burner 3 Heat storage type burner 5 Heat storage body 8 Combustion gas exhaust system which constitutes first exhaust means 10 Induction fan which constitutes first exhaust means 16 Second exhaust means
Claims (1)
熱体を備えると共に該蓄熱体を通して燃焼用空気の供給
及び燃焼ガスの排出を行なう蓄熱型バーナを少なくとも
1組炉体に設置し、これらバーナを交互に燃焼させて燃
焼させていない方のバーナから前記蓄熱体を経て燃焼ガ
スを排出させる第1の排気手段と、前記燃焼ガスを前記
バーナを通さずに炉外へ排出する第2の排気手段とを設
け、この第2の排気手段を操作することによって前記バ
ーナを通過する燃焼ガスの量を変化させて炉温を制御す
ることを特徴とする炉温制御方法。1. A heating furnace using a burner as a heat source, wherein at least one heat storage type burner is provided in the furnace body, the heat storage burner having a heat storage body and supplying combustion air and discharging combustion gas through the heat storage body. And a second exhaust means for discharging the combustion gas from the burner, which is not combusted, through the heat storage body, and the combustion gas is discharged outside the furnace without passing through the burner. Means for controlling the furnace temperature by changing the amount of combustion gas passing through the burner by operating the second exhaust means.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3050210A JPH0816529B2 (en) | 1991-02-25 | 1991-02-25 | Furnace temperature control method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3050210A JPH0816529B2 (en) | 1991-02-25 | 1991-02-25 | Furnace temperature control method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH04270819A JPH04270819A (en) | 1992-09-28 |
| JPH0816529B2 true JPH0816529B2 (en) | 1996-02-21 |
Family
ID=12852736
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP3050210A Expired - Fee Related JPH0816529B2 (en) | 1991-02-25 | 1991-02-25 | Furnace temperature control method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0816529B2 (en) |
Families Citing this family (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| TW338094B (en) * | 1996-05-22 | 1998-08-11 | Toyota Motor Co Ltd | Method and device of burning control of an oxygen sensor |
| JP4903083B2 (en) * | 2007-05-17 | 2012-03-21 | 新日鉄エンジニアリング株式会社 | Combustion control method for regenerative burner furnace |
| JP5131574B2 (en) * | 2010-10-05 | 2013-01-30 | 新東工業株式会社 | Exhaust gas purification device and temperature control method thereof |
| CN102207286B (en) * | 2011-03-18 | 2012-10-10 | 苏州安科节能技术有限公司 | Low-heating-value gas burner |
| CN102679731A (en) * | 2012-05-29 | 2012-09-19 | 无锡格莱德科技有限公司 | Heat storage type smelting furnace |
| CN102798142B (en) * | 2012-09-04 | 2015-12-09 | 王浩宇 | A kind of combustion control system |
| CN103062770A (en) * | 2013-01-16 | 2013-04-24 | 浙江大学 | High-temperature gas generating device on basis of porous medium combustion and heat storage |
-
1991
- 1991-02-25 JP JP3050210A patent/JPH0816529B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH04270819A (en) | 1992-09-28 |
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