JPH06265117A - Heating furnace - Google Patents
Heating furnaceInfo
- Publication number
- JPH06265117A JPH06265117A JP4955293A JP4955293A JPH06265117A JP H06265117 A JPH06265117 A JP H06265117A JP 4955293 A JP4955293 A JP 4955293A JP 4955293 A JP4955293 A JP 4955293A JP H06265117 A JPH06265117 A JP H06265117A
- Authority
- JP
- Japan
- Prior art keywords
- combustion
- chamber
- heating
- gas
- heating furnace
- 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.)
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Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、スラブ、ビレット、ブ
ルーム等の被加熱物を所定の目標温度まで加熱する加熱
炉、均熱炉、熱処理炉等一般的な加熱炉に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a general heating furnace such as a heating furnace, a soaking furnace and a heat treatment furnace for heating an object to be heated such as a slab, a billet and a bloom to a predetermined target temperature.
【0002】[0002]
【従来の技術】従来、この種の加熱炉は、燃料を空気で
燃焼して被加熱物の加熱を行う空気燃焼方式が一般的で
あったが、最近、燃料を純酸素もしくは酸素富化空気等
で燃焼して被加熱物の加熱を行う酸素燃焼方式が注目さ
れている。この酸素燃焼方式は従来の空気燃焼方式に対
して、燃焼ガス量が約1/4と少なく、炭酸ガス(CO
2 )と水蒸気(H2 O)の濃度が高いため、排ガス損失
熱の減少と炉内ガス放射電熱の増加による省エネ効果が
大であることに加えて、地球温暖化物質の炭酸ガスの回
収が容易という長所を有している。一方、この酸素燃焼
方式は、高温・高負荷燃焼のため、被加熱物の均一加熱
性が不良で、かつ、窒素酸化物(NOx )の濃度が高い
ため加熱炉へ適用できないという問題点があった。2. Description of the Related Art Heretofore, in this type of heating furnace, an air combustion method has been generally used in which a fuel is burned with air to heat an object to be heated. Recently, however, the fuel is pure oxygen or oxygen-enriched air. Attention has been paid to an oxy-fuel combustion method in which a material to be heated is burned by being burned by the above. Compared with the conventional air combustion method, this oxyfuel combustion method has a combustion gas amount of about 1/4, which is less than that of carbon dioxide gas (CO
2 ) and the concentration of water vapor (H 2 O) are high, the reduction of exhaust gas heat loss and the increase of radiant electric heat in the furnace have a great energy saving effect. It has the advantage of being easy. On the other hand, this oxyfuel combustion system has a problem that it cannot be applied to a heating furnace due to high temperature and high load combustion, poor uniform heating of the object to be heated, and high nitrogen oxide (NO x ) concentration. there were.
【0003】これに対して、例えば特開昭54−128
834号公報に示されているような加熱炉の燃焼方法が
ある。この技術の特徴は、酸素燃焼による高温熱ガスと
窒素酸化物の抑制を目的とし、これを達成するために、
図4に示すように、加熱炉1の低温の燃焼排ガスを循環
ファン18で昇圧して純酸素と混合した後、加熱炉1の
バーナ7に供給し、燃料と混合して燃焼に使用するもの
である。On the other hand, for example, JP-A-54-128
There is a heating furnace combustion method as disclosed in Japanese Patent No. 834. The feature of this technology is to suppress high temperature hot gas and nitrogen oxides due to oxygen combustion, and to achieve this,
As shown in FIG. 4, the low-temperature combustion exhaust gas of the heating furnace 1 is pressurized by the circulation fan 18 and mixed with pure oxygen, and then supplied to the burner 7 of the heating furnace 1 to be mixed with fuel and used for combustion. Is.
【0004】しかしながら、上記の燃焼方法では純酸素
を燃焼排ガスで稀釈して酸素濃度が21%の模擬空気と
して使用するため、従来の空気燃焼方式と同様に多数の
バーナと広い燃焼空気が必要となり、この結果、加熱炉
がコンパクト化出来ないという問題点があった。However, in the above combustion method, pure oxygen is diluted with combustion exhaust gas and used as simulated air having an oxygen concentration of 21%, so that a large number of burners and wide combustion air are required as in the conventional air combustion method. As a result, there is a problem that the heating furnace cannot be made compact.
【0005】[0005]
【発明が解決しようとする課題】本発明は、上記問題点
を解決すべく創案されたものであって、その目的は加熱
炉の低炉高化とバーナの集約により、加熱炉のコンパク
ト化と低コスト化を図った加熱炉を提供することにあ
る。SUMMARY OF THE INVENTION The present invention was devised to solve the above-mentioned problems, and its purpose is to make the heating furnace compact by increasing the low furnace height of the heating furnace and integrating burners. An object of the present invention is to provide a heating furnace whose cost is reduced.
【0006】[0006]
【課題を解決するための手段】本発明は、下記の事項を
要旨とするものである。 (1) 燃料を高濃度の酸素を含有した支燃ガスで燃焼
して被加熱物を加熱する加熱炉であって、その加熱炉が
燃料を燃焼する燃焼室と、その燃焼室で燃焼した燃焼ガ
スで被加熱物を加熱する加熱室とに区分されて設られて
いること。また、必要に応じて (2) 前記加熱室から前記燃焼室へ燃焼ガスを循環さ
せるための燃焼ガス循環炉を設けたこと。 (3) 前記過加熱室の両外側に隔壁で区分された前記
燃焼室を設けたこと。 (4) 加熱炉の煙道に炭酸ガス回収装置を配設し、前
記燃焼室から該炭酸ガス回収装置の上流側の煙道へ、燃
焼ガスを迂回させるための燃焼ガス迂回路を設けたこ
と。SUMMARY OF THE INVENTION The present invention is based on the following matters. (1) A heating furnace for heating an object to be heated by burning a fuel with a combustion-supporting gas containing a high concentration of oxygen, the combustion chamber in which the heating furnace burns the fuel, and the combustion in the combustion chamber. It must be installed separately from the heating chamber that heats the object to be heated with gas. If necessary, (2) a combustion gas circulation furnace for circulating combustion gas from the heating chamber to the combustion chamber is provided. (3) The combustion chambers divided by partition walls are provided on both outsides of the overheating chamber. (4) A carbon dioxide gas recovery device is provided in the flue of the heating furnace, and a combustion gas bypass circuit for diverting the combustion gas from the combustion chamber to the flue gas upstream of the carbon dioxide recovery device is provided. .
【0007】本発明の加熱炉は、従来の加熱炉を燃焼室
と加熱室に機能分割した構成のため、燃焼室で燃料の高
負荷・量論(理論)燃焼ができ、加熱室は炭酸ガスと水
蒸気の濃度に反比例して炉高が低く出来る。また、加熱
室と燃焼室の間で低温の燃焼ガスの循環を行うため、酸
素燃焼時の高温燃焼ガスと窒素酸化物が抑制出来る。ま
た、加熱室の両外側に隔壁で区分された燃焼室を設けて
いるため、炉壁が減少して設備コストと炉体放射熱が減
少出来る。さらに、燃焼室の燃焼ガスを迂回路で炭酸ガ
ス回収装置に直送できるため、加熱炉の操業負荷に関係
なく炭酸ガスの回収量を一定に出来る。Since the heating furnace of the present invention has a structure in which the conventional heating furnace is divided into a combustion chamber and a heating chamber, a high load and stoichiometric (theoretical) combustion of fuel can be carried out in the combustion chamber, and the heating chamber has carbon dioxide gas. And the furnace height can be lowered in inverse proportion to the steam concentration. Further, since the low temperature combustion gas is circulated between the heating chamber and the combustion chamber, the high temperature combustion gas and the nitrogen oxides at the time of oxygen combustion can be suppressed. Further, since the combustion chambers divided by the partition walls are provided on both outer sides of the heating chamber, the furnace wall is reduced and the facility cost and the radiant heat of the furnace body can be reduced. Furthermore, since the combustion gas in the combustion chamber can be directly sent to the carbon dioxide recovery device by a bypass, the amount of carbon dioxide recovered can be made constant regardless of the operating load of the heating furnace.
【0008】[0008]
【実施例】以下に、本発明を実施例に基づいてより詳細
に説明する。図1、および図2に示すごとく、耐火物の
炉壁で形成した加熱炉1内に耐火物の隔壁2を設けて燃
焼室3と加熱室4を構成し、この燃焼室3と加熱室4の
両端を燃焼ガス供給路5と燃焼ガス循環路6で連結す
る。また、燃焼室3の一端側にバーナ7を配置して燃料
供給管8と支燃ガス供給管9を接続し、燃料と支燃ガス
を供給して燃焼室3内で燃料の酸素燃焼を行う。EXAMPLES The present invention will now be described in more detail based on examples. As shown in FIGS. 1 and 2, a partition wall 2 of a refractory material is provided in a heating furnace 1 formed of a furnace wall of the refractory material to form a combustion chamber 3 and a heating chamber 4. Both ends of are connected by a combustion gas supply path 5 and a combustion gas circulation path 6. Further, a burner 7 is arranged at one end side of the combustion chamber 3 to connect a fuel supply pipe 8 and a combustion-supporting gas supply pipe 9 to supply fuel and combustion-supporting gas to perform oxygen combustion of the fuel in the combustion chamber 3. .
【0009】燃料としては、一般に気体もしく液体状の
各種燃料が使用可能であるが、窒素酸化物の抑制と炭酸
ガスの回収を行う場合は、燃料中に窒素(N)分等の不
純物の無い液化天然ガス(LNG)、液化石油ガス(L
PG)等の使用が望ましい。また、ここでいう「支燃ガ
ス」とは、高濃度の酸素(O2 )を含有した純酸素、酸
素富化空気、排ガス稀釈の酸素ガス等の総称である。As the fuel, various gas or liquid fuels can be generally used. However, in the case of suppressing nitrogen oxides and recovering carbon dioxide gas, impurities such as nitrogen (N) are contained in the fuel. Liquefied natural gas (LNG), liquefied petroleum gas (L)
PG) or the like is preferable. Further, the "flammable gas" as used herein is a general term for pure oxygen containing a high concentration of oxygen (O 2 ), oxygen-enriched air, oxygen gas diluted with exhaust gas, and the like.
【0010】一方、加熱室4の両端に仕切り壁10を設
けて燃焼ガスの加熱室4内への均等分配を図り、この燃
焼ガスのガス放射伝達でバーナ7側から加熱室4内に装
入された被加熱物11を加熱する。さらに、加熱炉1の
炉長方向のバーナ7側に排ガスの煙道12を設け、この
煙道12にガス冷却器13a、ダンパー14a、誘引ブ
ロウ15、炭酸ガス回収装置16を配置する。また、燃
焼室3と炭酸ガス回収装置16の上流側の煙道12を燃
焼ガス迂回路17で連結し、この燃焼ガス迂回路17に
ガス冷却器13b、ダンパー14bを配置する。On the other hand, partition walls 10 are provided at both ends of the heating chamber 4 to evenly distribute the combustion gas into the heating chamber 4, and the combustion gas is transferred into the heating chamber 4 from the burner 7 side by gas radiation transmission. The heated object 11 thus heated is heated. Further, an exhaust gas flue 12 is provided on the burner 7 side in the furnace length direction of the heating furnace 1, and a gas cooler 13a, a damper 14a, an induction blower 15, and a carbon dioxide recovery device 16 are arranged in the flue 12. Further, the combustion chamber 3 and the flue 12 on the upstream side of the carbon dioxide recovery device 16 are connected by a combustion gas bypass 17, and a gas cooler 13b and a damper 14b are arranged in the combustion gas bypass 17.
【0011】次に、本発明に係る加熱炉の作動機能につ
いて説明する。まず、バーナ7に燃料と支燃ガスを供給
して、燃焼室3内で燃料の酸素燃焼をを行う。この結
果、酸素燃焼による高負荷燃焼と燃焼ガス量の低減によ
り、バーナ7の集約と燃焼室3のコンパクト化が出来
る。一方、バーナ7の流体噴出エネルギーを利用して、
加熱室4から低温の燃焼ガスを誘引し、高温の酸素燃焼
ガスの稀釈を行い、被加熱物11の加熱に適した燃焼ガ
ス温度に調整する。Next, the operating function of the heating furnace according to the present invention will be described. First, the fuel and the combustion-supporting gas are supplied to the burner 7, and the fuel is oxy-combusted in the combustion chamber 3. As a result, the burners 7 can be integrated and the combustion chamber 3 can be made compact by high-load combustion and reduction of the amount of combustion gas by oxyfuel combustion. On the other hand, using the fluid ejection energy of the burner 7,
A low temperature combustion gas is attracted from the heating chamber 4, a high temperature oxygen combustion gas is diluted, and a combustion gas temperature suitable for heating the object 11 is adjusted.
【0012】この燃焼ガスを加熱室4に均一に分配して
被加熱物11の加熱を行うが、酸素燃焼であるので炭酸
ガスと水蒸気の濃度が空気燃焼に対して約4倍高いた
め、加熱室4の炉高を約1/4にしても、空気燃焼とほ
ぼ同一の被加熱物11の加熱が可能である。また、高濃
度の炭酸ガスを回収して外販する場合、燃焼室3と煙道
12の間に燃焼ガス迂回路17を設けてあるため、加熱
炉1の操業負荷に関係なくバーナ7を燃焼出来るので炭
酸ガスの回収量が一定となる。図中の矢線は燃焼ガスの
流れを示し、二重矢線は被加熱物11の移動方向を示
す。This combustion gas is evenly distributed to the heating chamber 4 to heat the object 11 to be heated, but since it is oxygen combustion, the concentration of carbon dioxide and water vapor is about four times higher than that of air combustion, so heating is performed. Even if the furnace height of the chamber 4 is set to about 1/4, it is possible to heat the object 11 to be heated almost the same as air combustion. Further, when the high-concentration carbon dioxide gas is collected and sold to the outside, since the combustion gas bypass 17 is provided between the combustion chamber 3 and the flue 12, the burner 7 can be burned regardless of the operation load of the heating furnace 1. Therefore, the recovery amount of carbon dioxide becomes constant. Arrows in the figure show the flow of combustion gas, and double arrows show the moving direction of the object to be heated 11.
【0013】本発明は、上記実施例にのみ限定されるも
のではなく、例えば、 (1) 燃焼室3と加熱室4をシリーズに連結すること (2) 燃焼室3と加熱室4の炉体を分離構造とするこ
と (3) 図3に示すように、燃焼室3と加熱室4のユニ
ットを炉長方向にシリーズに連結して多帯化すること (4) 燃焼室3の炉長方向に多段で支燃ガスを供給し
て多段燃焼を行うこと (5) 燃焼室3の出口部で燃焼ガス組成を検知して量
論燃焼を行うこと等も可能であり、本発明の要旨を逸脱
しない限り、種々変更を加え得ることは勿論可能であ
る。The present invention is not limited to the above-mentioned embodiment, but includes, for example, (1) connecting the combustion chamber 3 and the heating chamber 4 in series (2) the furnace body of the combustion chamber 3 and the heating chamber 4. (3) As shown in FIG. 3, the units of the combustion chamber 3 and the heating chamber 4 are connected in series in the furnace length direction to form multiple zones (4) The combustion chamber 3 in the furnace length direction (5) It is also possible to detect stoichiometric combustion by detecting the composition of the combustion gas at the outlet of the combustion chamber 3 and to carry out multi-stage combustion by supplying the combustion-supporting gas to the multi-stage combustion gas. It is of course possible to make various changes unless they are done.
【0014】[0014]
【発明の効果】本発明の加熱炉によれば、下記の優れた
効果を奏するものである。 (1) 酸素燃焼式で燃焼室と加熱室に機能分割した構
成のため、高負荷燃焼により燃焼室のコンパクト化とバ
ーナの集約化が出来る。また、高濃度の放射ガスにより
加熱室のコンパクト化が出来る。 (2) 燃焼室と加熱室の間で低温の燃焼ガス循環を行
うため、酸素燃焼特有の高温燃焼と窒素酸化物の抑制が
出来る。 (3) 加熱室の両外側に隔壁で区分された燃焼室を設
けているため、炉壁が減少して設備コストと炉体放射熱
が減少出来る。 (4) 燃焼室と煙道の間に燃焼ガス迂回路を設けたた
め、加熱炉の操業負荷に関係なく炭酸ガスの回収量を一
定に出来る。 (5) さらに、燃焼室で量論燃焼が出来るため酸素の
消費量が低減できると共に、窒素酸化物とスケールの生
成が抑制できる。According to the heating furnace of the present invention, the following excellent effects are exhibited. (1) Since the function is divided into the combustion chamber and the heating chamber by the oxyfuel combustion type, the combustion chamber can be made compact and the burner can be integrated by high-load combustion. In addition, the heating chamber can be made compact due to the high-concentration radiation gas. (2) Since low-temperature combustion gas is circulated between the combustion chamber and the heating chamber, it is possible to suppress high-temperature combustion and nitrogen oxides peculiar to oxygen combustion. (3) Since the combustion chambers divided by partition walls are provided on both outsides of the heating chamber, the furnace wall is reduced, and the equipment cost and the radiant heat of the furnace body can be reduced. (4) Since the combustion gas bypass is provided between the combustion chamber and the flue, the carbon dioxide recovery amount can be kept constant regardless of the operating load of the heating furnace. (5) Furthermore, since stoichiometric combustion can be performed in the combustion chamber, the consumption of oxygen can be reduced and the production of nitrogen oxides and scales can be suppressed.
【図1】本発明に係る加熱炉の実施例を示す平面図。FIG. 1 is a plan view showing an embodiment of a heating furnace according to the present invention.
【図2】図1をA−A面で切った加熱炉の縦断面図。FIG. 2 is a vertical cross-sectional view of the heating furnace taken along the line AA in FIG.
【図3】本発明の加熱炉の他の実施例を示す平面図。FIG. 3 is a plan view showing another embodiment of the heating furnace of the present invention.
【図4】従来技術を示す加熱炉の概念図。FIG. 4 is a conceptual diagram of a heating furnace showing a conventional technique.
1 加熱炉 2 隔壁 3 燃焼室 4 加熱室 5 燃焼ガス供給路 6 燃焼ガス循環路 7 バーナ 8 燃焼供給管 9 支燃ガス供給管 10 仕切り壁 11 被加熱物 12 煙道 13a,13b ガス冷却器 14a,14b ダンパー 15 誘引ブロウ 16 炭酸ガス回収装置 17 燃焼ガス迂回路 18 循環ファン 19 純酸素供給管 1 Heating Furnace 2 Partition 3 Combustion Chamber 4 Heating Chamber 5 Combustion Gas Supply Path 6 Combustion Gas Circulation Path 7 Burner 8 Combustion Supply Pipe 9 Combustion Gas Supply Pipe 10 Partition Wall 11 Heated Object 12 Flue 13a, 13b Gas Cooler 14a , 14b Damper 15 Induction blow 16 Carbon dioxide recovery device 17 Combustion gas bypass 18 Circulation fan 19 Pure oxygen supply pipe
Claims (4)
燃焼して被加熱物の加熱を行う加熱炉であって、その加
熱炉を燃料を燃焼する燃焼室と、その燃焼室で燃焼した
燃焼ガスで被加熱物を加熱する加熱室、とに区分して設
けたことを特徴とする加熱炉。1. A heating furnace for burning an object to be heated by burning a fuel with a combustion-supporting gas containing a high concentration of oxygen, comprising: a combustion chamber for burning the fuel in the heating furnace; A heating furnace characterized by being divided into a heating chamber for heating an object to be heated by the combustion gas burned.
環させるための燃焼ガス循環炉を設けたことを特徴とす
る請求項1記載の加熱炉。2. The heating furnace according to claim 1, further comprising a combustion gas circulating furnace for circulating a combustion gas from the heating chamber to the combustion chamber.
記燃焼室を設けたことを特徴とする請求項1、2記載の
加熱炉。3. The heating furnace according to claim 1, wherein the combustion chambers divided by partition walls are provided on both outer sides of the heating chamber.
し、前記燃焼室から該炭酸ガス回収装置の上流側の煙道
へ、燃焼ガスを迂回させるための燃焼ガス迂回路を設け
たことを特徴とする請求項1、2、3記載の加熱炉。4. A carbon dioxide gas recovery device is provided in a flue of a heating furnace, and a combustion gas bypass circuit for diverting combustion gas from the combustion chamber to a flue upstream of the carbon dioxide gas recovery device is provided. The heating furnace according to claim 1, 2, or 3, characterized in that.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4955293A JPH06265117A (en) | 1993-03-10 | 1993-03-10 | Heating furnace |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4955293A JPH06265117A (en) | 1993-03-10 | 1993-03-10 | Heating furnace |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH06265117A true JPH06265117A (en) | 1994-09-20 |
Family
ID=12834364
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP4955293A Withdrawn JPH06265117A (en) | 1993-03-10 | 1993-03-10 | Heating furnace |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH06265117A (en) |
-
1993
- 1993-03-10 JP JP4955293A patent/JPH06265117A/en not_active Withdrawn
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