JPS5812326B2 - Continuous heating furnace - Google Patents
Continuous heating furnaceInfo
- Publication number
- JPS5812326B2 JPS5812326B2 JP55074928A JP7492880A JPS5812326B2 JP S5812326 B2 JPS5812326 B2 JP S5812326B2 JP 55074928 A JP55074928 A JP 55074928A JP 7492880 A JP7492880 A JP 7492880A JP S5812326 B2 JPS5812326 B2 JP S5812326B2
- Authority
- JP
- Japan
- Prior art keywords
- heating
- zone
- combustion
- air
- supply pipe
- 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
Links
Landscapes
- Heat Treatments In General, Especially Conveying And Cooling (AREA)
- Tunnel Furnaces (AREA)
Description
【発明の詳細な説明】
本発明は分塊圧延された鋼片または連続鋳造された鋼片
等を熱間圧延するために所定温度まで再加熱する型式の
連続式加熱炉、殊に3帯式の連続式加熱炉に係るもので
ある。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a continuous heating furnace of the type that reheats a bloom-rolled steel billet or a continuously cast steel billet to a predetermined temperature for hot rolling, particularly a three-zone type. This relates to a continuous heating furnace.
従来、前記種類の連続式加熱炉において、鋼片を圧延可
能な温度まで加熱昇温させる場合、過剰空気率の大小に
よって差異は生ずるが、一般にはバーナの燃焼を容易に
して火炎を安定せしめるのに多少過剰空気率で燃焼させ
ているのが現状であり、このだめに鋼片の表面酸化によ
る損失を免れることができないという欠点がある。Conventionally, in the above-mentioned type of continuous heating furnace, when heating a steel billet to a temperature at which it can be rolled, differences occur depending on the amount of excess air, but in general, it is necessary to facilitate combustion in the burner and stabilize the flame. Currently, combustion is carried out with a somewhat excess air content, which has the disadvantage that losses due to surface oxidation of the steel slab cannot be avoided.
これに対して、本発明は前記欠点を除去し得る連続式加
熱炉を提供しようとするものであって、その要旨とする
ところは、鋼片を圧延温度まで加熱する加熱帯と該鋼片
のスキツドマークを減少して当該温度が均一になるよう
に加熱する均熱帯とが明確に区分されている型式の連続
式加熱炉において、前記均熱帯におけるバーナー燃焼を
不完全燃焼状態になすことによって前記鋼片の酸化損失
を防止すると共に、前記不完全燃焼による燃油分は前記
加熱帯に当該不足分の空気量を加えて二次燃焼を起させ
ることにより完全燃焼状態になす点に存するものであり
、また当該装置の要旨とするところは、鋼片を圧延温度
まで加熱する加熱帯と該鋼片のスキツドマークを減少し
て当該温度が均一になるように加熱する均熱帯とが明確
に区分されている型式の連続式加熱炉において、前記加
熱帯を加熱すべき上部燃焼バーナーの空気供給管から分
岐空気供給管をバイパスさせ、該分岐空気供給管にフレ
キシブルホースを介して接続されるべき空気噴射管を前
記加熱帯と前記均熱帯との接続炉壁部分に空気噴出がで
きるように設けた点に存するものであり、かくして、本
発明によれば、炉内の均熱帯におけるバーナ燃焼を不完
全燃焼状態となすことによって鋼片の表面酸化による損
失を防止することができると共に、この不完全燃焼状態
による燃油分は加熱帯に不足分の空気を加えて二次燃焼
させて完全燃焼せしめることによって余剰燃油分を有効
に利用できることから省エネルギ一対策に充分貢献し得
て経済的である。In contrast, the present invention aims to provide a continuous heating furnace capable of eliminating the above-mentioned drawbacks, and the gist of the present invention is to provide a heating zone for heating a steel billet to a rolling temperature, and a heating zone for heating a steel billet to a rolling temperature. In a type of continuous heating furnace that is clearly separated from a soaking zone where heating is performed to reduce skid marks and make the temperature uniform, the steel is heated by bringing the burner combustion in the soaking zone into an incomplete combustion state. In addition to preventing oxidation loss of the pieces, the fuel oil due to the incomplete combustion is brought into a complete combustion state by adding the insufficient amount of air to the heating zone to cause secondary combustion, In addition, the gist of this equipment is that the heating zone that heats the steel slab to rolling temperature and the soaking zone that heats the steel slab to reduce skid marks and make the temperature uniform are clearly separated. In this type of continuous heating furnace, a branch air supply pipe is bypassed from the air supply pipe of the upper combustion burner which is to heat the heating zone, and an air injection pipe to be connected to the branch air supply pipe via a flexible hose is provided. The present invention consists in that the furnace wall portion connecting the heating zone and the soaking zone is provided so that air can be blown out.Thus, according to the present invention, the burner combustion in the soaking zone in the furnace is brought into an incomplete combustion state. By doing so, it is possible to prevent loss due to surface oxidation of the steel billet, and the remaining amount of fuel due to incomplete combustion can be recovered by adding air to the heating zone to cause secondary combustion and complete combustion. It is economical because it can fully contribute to energy saving measures because it can effectively utilize the energy.
次に、第1図乃至第3図に示されている二実施例により
本発明を更に詳細に説明する。Next, the present invention will be explained in more detail with reference to two embodiments shown in FIGS. 1 to 3.
先ず、本発明の第一実施例が示されている第1図におい
て、1は加熱炉本体、2は予熱帯、3は加熱帯、4は均
熱帯、5は煙道をそれぞれ示すものであって、予熱帯2
及び加熱帯3には自体周知のように冷却水が通過乃至楯
環せしめられているスキツドパイプ6及びクロスパー7
を設け、分塊圧延または連続鋳造された鋼片8は加熱サ
イクルに応じた設定温度に滞留させる時間に対応した速
さで第2図に示されているスキツドパイプ6の頂部に軸
線方向に固設してあるスキツドレール9上を移送される
ものであり、また、前記加熱サイクルの温度設定を保持
するために、加熱帯3には上部燃焼バーナー10及び下
部燃焼バーナー11が、均熱帯4には他の燃焼バーナー
12がそれぞれ設置してある。First, in FIG. 1, which shows the first embodiment of the present invention, 1 is a heating furnace main body, 2 is a preheating zone, 3 is a heating zone, 4 is a soaking zone, and 5 is a flue. So, preheating zone 2
In addition, the heating zone 3 includes a skid pipe 6 and a cross spar 7 through which cooling water passes or is shielded, as is well known in the art.
The slab-rolled or continuously cast steel billet 8 is fixed in the axial direction at the top of the skid pipe 6 shown in FIG. 2 at a speed corresponding to the residence time at the set temperature corresponding to the heating cycle. In addition, in order to maintain the temperature setting of the heating cycle, an upper combustion burner 10 and a lower combustion burner 11 are installed in the heating zone 3, and other combustion burners are installed in the soaking zone 4. Combustion burners 12 are installed respectively.
更に、第2図に示すように、上部燃焼バーナー10に通
ずる空気供給管13からバイパスした分岐空気供給管1
4は一端が加熱帯3と均熱帯4との境界面となる彎曲〆
壁部分15近傍に埋設されるべき空気噴射管16の他端
にフレキシブルホース17を介して接続されており、か
くして、鋼片8の表面温度が最高温度になって加熱炉本
体1内を通過する時間の約1/2〜1/3に相当するゾ
ーン即ち均熱帯4におけるバーナー12による燃焼状態
を空気不足の不完全燃焼となすことによって前記鋼片の
酸化損失を防止すると共に、この不完全燃焼による余剰
の燃油分は、空気供給管13からの燃焼用空気を適宜バ
ルブを調節してその不足分空気量だけを分岐空気供給管
14及びフレキシブルホース17を経て噴射管16から
鋼片8の進行方向斜め前方から噴出せしめて二次燃焼さ
せることにより完全燃焼を行なうものである。Furthermore, as shown in FIG. 2, a branch air supply pipe 1 bypassed from the air supply pipe 13 leading to the upper combustion burner 10
4 has one end connected via a flexible hose 17 to the other end of an air injection pipe 16 to be buried in the vicinity of the curved finishing wall portion 15 that forms the interface between the heating zone 3 and the soaking zone 4. The combustion state by the burner 12 in the soaking zone 4, which corresponds to about 1/2 to 1/3 of the time during which the surface temperature of the piece 8 reaches its maximum temperature and passes through the heating furnace main body 1, is incomplete combustion due to lack of air. By doing so, oxidation loss of the steel billets is prevented, and excess fuel due to this incomplete combustion is diverted from the combustion air from the air supply pipe 13 by appropriately adjusting the valve to divert only the insufficient amount of air. Complete combustion is achieved by injecting the steel pieces 8 from the injection pipe 16 diagonally forward in the traveling direction of the steel pieces 8 through the air supply pipe 14 and the flexible hose 17, and causing secondary combustion.
なお、1Bは鋼片8の装入側扉、19は同抽出側扉、2
0は耐火物の取付アンカー、21は支持梁で、前記取付
アンカーは秩線22等にて支持パイプ23に固着され、
上部燃焼バーナー10(下部燃焼バーナー11及び燃焼
バーナー12)は公知のように前板24及びバーナータ
イル25に装着される。In addition, 1B is the charging side door of the steel billet 8, 19 is the same extraction side door, 2
0 is a refractory installation anchor, 21 is a support beam, and the installation anchor is fixed to a support pipe 23 with a wire 22 or the like,
The upper combustion burner 10 (lower combustion burner 11 and combustion burner 12) is mounted to the front plate 24 and the burner tile 25 in a known manner.
次に、第3図は本発明の第二実施例を示すものであって
、叙上の第一実施例では噴射管16からの噴射空気流が
鋼片8の進行方向斜め前方から当るようになっているが
、本実施例では噴射空気流が鋼片8の進行方向に対して
逆となるように前記空気噴射管を均熱帯4の縮小炉壁部
分26に設け且つその先端に変向ノズル27が装着して
ある。Next, FIG. 3 shows a second embodiment of the present invention, and in the first embodiment described above, the jet air flow from the jet pipe 16 hits the steel billet 8 obliquely from the front in the advancing direction. However, in this embodiment, the air injection pipe is provided in the reduced furnace wall portion 26 of the soaking zone 4 so that the injection air flow is opposite to the advancing direction of the steel billet 8, and a direction changing nozzle is provided at the tip of the air injection pipe. 27 is installed.
次に、前記構成を有する連続式加熱炉の操業態様につい
て述べると、装入側扉18を開いてブツシャー等の搬送
人手段にてスキツドパイプ6のスキツドレール9上に搬
入せしめられた鋼片8は順次搬送されながらそれぞれの
設定温度に保持されている予熱帯(700〜SOOC)
、鋼片8を圧延可能温度まで加熱する加熱帯(1250
g1300℃)及び前記鋼片のスキツドマークを減少し
て当該温度が均一になるように加熱する均熱帯(約12
00℃)を通過するものであるが、この場合、加熱帯3
において、1200〜1250℃に昇温せしめられた鋼
片8は均熱帯4を通過した後、抽出側扉19から約11
50℃の保有温度で圧延工程へと移される。Next, the operation mode of the continuous heating furnace having the above configuration will be described. The charging side door 18 is opened and the steel slabs 8 are sequentially carried onto the skid rail 9 of the skid pipe 6 by carrier means such as a butcher. Preheating zone (700~SOOC) maintained at each set temperature while being transported
, a heating zone (1250
g1300℃) and a soaking zone (approximately 12
00℃), but in this case, heating zone 3
After passing through the soaking zone 4, the steel piece 8 heated to 1200 to 1250°C passes through the extraction side door 19 for approximately 11 minutes.
It is transferred to the rolling process at a holding temperature of 50°C.
しかして、本発明によれば、領片8の表面酸化損失を防
止するために、均熱帯4におけるバーナー12の燃焼空
気不足(理論空気量の70〜90%の空気)による不完
全燃焼状態となし、これによって生ずる燃油分は彎曲炉
壁部分15または縮小炉壁部分26に設けた噴射管16
から不足分の空気量を加えてバーナーio,i1による
二次燃焼を起させて完全燃焼させるものである。According to the present invention, in order to prevent surface oxidation loss of the area piece 8, an incomplete combustion state due to a lack of combustion air (70 to 90% of the theoretical air amount) of the burner 12 in the soaking zone 4 is prevented. None, the resulting fuel is sent to the injection pipe 16 provided on the curved furnace wall section 15 or the reduced furnace wall section 26.
The insufficient amount of air is added to cause secondary combustion by burners io and i1, resulting in complete combustion.
第1図は本発明に係る連続式加熱炉の一例を示す長手方
向縦断面図、第2図及び第3図は本発明の異なる実施例
を示す第1図のA部拡大詳細図である。
なお、図示された主要部と符号との対応関係は下記の通
りである。
1・・・・・・加熱炉本体、2・・・・・・予熱帯、3
・・・・・・加熱帯、4・・・・・・均熱帯、6・・・
・・・スキツドパイプ、8・・・・・・鋼片、9・・・
・・・スキツドレール、10・・・・・・上部燃焼バー
ナー、11・・・・・・下部燃焼バーナー、12・・・
・・燃焼バーナー、13・・・・・・空気供給管、14
・・・・・・分岐空気供給管、15 彎曲炉壁部分、
16・・・・・・空気噴射管、17・・・・・・フレキ
ンプルホース、26・・・・・傭小炉壁部分。FIG. 1 is a longitudinal cross-sectional view showing an example of a continuous heating furnace according to the present invention, and FIGS. 2 and 3 are enlarged detailed views of section A in FIG. 1 showing different embodiments of the present invention. Note that the correspondence relationship between the main parts shown and the symbols is as follows. 1...Heating furnace main body, 2...Pre-heating zone, 3
... Heating zone, 4... Soaking zone, 6...
... skid pipe, 8 ... steel piece, 9 ...
... skid rail, 10 ... upper combustion burner, 11 ... lower combustion burner, 12 ...
... Combustion burner, 13 ... Air supply pipe, 14
...Branch air supply pipe, 15 curved furnace wall section,
16... Air injection pipe, 17... Frekin pull hose, 26... Small furnace wall part.
Claims (1)
ツドマークを減少して当該温度が均一になるように加熱
する均熱帯とが、明確に区分されている型式の連続式加
熱炉において、前記加熱帯を加熱すべき上部燃焼バーナ
ーの空気供給管から分岐空気供給管をバイパスさせ、該
分岐空気供給管にフレキシブルホースを介して接続され
るべき空気噴射管を前記加熱帯と前記均熱帯との接続炉
壁部分に空気噴出ができるように設けたことを特徴とす
る連続式加熱炉。1. In a continuous heating furnace of a type in which a heating zone for heating the steel slab to the rolling temperature and a soaking zone for heating the steel slab to reduce skid marks and uniformize the temperature are clearly separated. A branch air supply pipe is bypassed from the air supply pipe of the upper combustion burner that is to heat the heating zone, and an air injection pipe to be connected to the branch air supply pipe via a flexible hose is connected to the heating zone and the soaking zone. A continuous heating furnace characterized by having a connecting furnace wall section so that air can be blown out.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP55074928A JPS5812326B2 (en) | 1980-06-05 | 1980-06-05 | Continuous heating furnace |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP55074928A JPS5812326B2 (en) | 1980-06-05 | 1980-06-05 | Continuous heating furnace |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS572820A JPS572820A (en) | 1982-01-08 |
| JPS5812326B2 true JPS5812326B2 (en) | 1983-03-08 |
Family
ID=13561500
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP55074928A Expired JPS5812326B2 (en) | 1980-06-05 | 1980-06-05 | Continuous heating furnace |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5812326B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6440742U (en) * | 1987-09-04 | 1989-03-10 |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0248472Y2 (en) * | 1986-02-17 | 1990-12-19 | ||
| JP3777204B2 (en) | 1994-11-11 | 2006-05-24 | 日精エー・エス・ビー機械株式会社 | Heat-resistant container molding apparatus and molding method |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5339848B2 (en) * | 1973-02-28 | 1978-10-24 | ||
| JPS5147404A (en) * | 1974-10-22 | 1976-04-23 | Clarion Co Ltd | TEEPUJIDOTEISHIJINIOKERU MOOTAKIDOSOCHI |
| JPS53137009A (en) * | 1977-05-04 | 1978-11-30 | Nippon Steel Corp | Non-oxidation furnace of direct firing type |
-
1980
- 1980-06-05 JP JP55074928A patent/JPS5812326B2/en not_active Expired
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6440742U (en) * | 1987-09-04 | 1989-03-10 |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS572820A (en) | 1982-01-08 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US2362085A (en) | Method of heating open-hearth furnace charges | |
| US3819323A (en) | Minimum scale reheating furnace and means relating thereto | |
| JPS5812326B2 (en) | Continuous heating furnace | |
| CN101775483A (en) | Heat accumulative roller bottom heating furnace | |
| US3836320A (en) | Minimum scale reheating furnace and means relating thereto | |
| US2329211A (en) | Continuous heating furnace and method of operating the same | |
| US3022057A (en) | Direct-heating oven | |
| CN210481468U (en) | Chain grate machine concurrent heating system that is fit for iron ore concentrate production | |
| US1983927A (en) | Open hearth furnace operation | |
| CN101435018B (en) | Hot dip galvanizing annealing process and high temperature annealing furnace | |
| US5257804A (en) | Device for igniting a bed of a mixture of materials such as ore and coke | |
| US2126272A (en) | Open hearth furnace | |
| JPS5597422A (en) | Fast heating appartaus for continuous annealing installation | |
| US3322578A (en) | Thermochemical desurfacing method | |
| JPS6238410B2 (en) | ||
| GB302651A (en) | Improvements in apparatus for heating billets and the like | |
| SU1359307A1 (en) | Method of heating open-hearth furnace | |
| JPS6138905Y2 (en) | ||
| JPH07258740A (en) | Method and apparatus for continuously heating billets | |
| JPS63109113A (en) | Heating device in heating furnace | |
| US1999854A (en) | Method of welding | |
| JPS58192668A (en) | Heater for end part of ingot | |
| SU620774A1 (en) | Two-tank steel-making furnace | |
| JP3174148B2 (en) | Furnace equipment for heating and soaking high-temperature slabs | |
| SU1183803A1 (en) | Furnace for article heating |