JPS5873727A - Preheating method of strip in continuous heat treatment equipment - Google Patents
Preheating method of strip in continuous heat treatment equipmentInfo
- Publication number
- JPS5873727A JPS5873727A JP17070181A JP17070181A JPS5873727A JP S5873727 A JPS5873727 A JP S5873727A JP 17070181 A JP17070181 A JP 17070181A JP 17070181 A JP17070181 A JP 17070181A JP S5873727 A JPS5873727 A JP S5873727A
- Authority
- JP
- Japan
- Prior art keywords
- strip
- heating furnace
- furnace
- heating
- heating medium
- 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
Classifications
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21D—MODIFYING 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
- C21D9/00—Heat treatment, e.g. annealing, hardening, quenching or tempering, adapted for particular articles; Furnaces therefor
- C21D9/52—Heat treatment, e.g. annealing, hardening, quenching or tempering, adapted for particular articles; Furnaces therefor for wires; for strips ; for rods of unlimited length
- C21D9/54—Furnaces for treating strips or wire
- C21D9/56—Continuous furnaces for strip or wire
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 Treatment Of Strip Materials And Filament Materials (AREA)
- Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は連続熱処理設備におけるストリップの予熱方法
に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for preheating a strip in a continuous heat treatment facility.
連続焼鈍炉等のストリップの連続熱処理設備では、はは
空温状態のス)IJツブを数百度まで加熱する必要があ
り、このため加熱炉には極めて大色な熱量が導入される
。In continuous heat treatment equipment for strips such as a continuous annealing furnace, it is necessary to heat the air-temperature IJ tube to several hundred degrees, and for this reason, an extremely large amount of heat is introduced into the heating furnace.
しかしながら、このような加熱炉内の燃焼熱のうち、実
際にストリップの加熱のために用いられる熱は全体の申
分程度であシ、40〜sobの燃焼熱は燃焼排ガスによ
る熱損失となるのが通常である。このよう゛なことから
従来加熱炉内の燃焼熱の有効利用を図り燃料原単位を低
減せしめるため、加熱炉の燃焼排ガスを加熱炉の前面で
ストリップ表面KvKき付けることにjpストリップの
予熱を行う方法が提案されている。しかし、この方法で
は熱の利用効率という面ではそれなシO効果を期待でき
るものの、これを実施するためには加熱炉の前面に別の
もう1)C)炉を設けなければならないという設備上O
問題があるとともに、排ガスを直接ストリップ表面に吹
き付は九場合、ス)971表面の性状を劣化させてしま
うという問題を有している。However, of the combustion heat in such a heating furnace, the heat actually used for heating the strip is only about the entire amount, and the combustion heat of 40 to sob becomes heat loss due to combustion exhaust gas. is normal. For this reason, conventionally, in order to effectively utilize the combustion heat in the heating furnace and reduce the fuel consumption rate, the strip is preheated by applying the combustion exhaust gas of the heating furnace to the strip surface KvK at the front of the heating furnace. A method is proposed. However, although this method can be expected to have a certain effect in terms of heat utilization efficiency, in order to implement this method, another (C) furnace must be installed in front of the heating furnace. O
Another problem is that if the exhaust gas is directly blown onto the strip surface, the properties of the 971 surface deteriorate.
本発明は以上のような従来の問題を解決せんとして創案
されたもので、コンパクトな設備で、しかもストリップ
の品質に悪影響を及ばずことなく加熱炉の燃焼排ガスの
顕熱を利用してストリップを予熱することができゐ方法
を提供せんとするものである。本発明は、加熱炉人情に
設けられた通板ロール内に加熱炉の燃焼排ガスの顕熱を
熱交換装置にょシ回収せしめた高沸点有機熱媒を流通せ
しめ、この高沸点有機熱媒によル前記通板ロールを介し
てストリップを予熱するようKしたものであり、かくす
ることによシ、大損シな設備を賛することなく、シかも
ストリップの品質に何らの悪影醤を及ばずことなく、燃
焼排ガスの顕熱を利用し九ストリップの予熱が可能とな
る。The present invention was devised to solve the above-mentioned conventional problems, and it is possible to process strips using sensible heat of combustion exhaust gas from a heating furnace with compact equipment and without adversely affecting the quality of the strips. The purpose is to provide a method for preheating. The present invention circulates a high boiling point organic heating medium in which the sensible heat of the combustion exhaust gas of the heating furnace is recovered by a heat exchanger through a passing roll installed in the heating furnace. The strip is preheated through the threading roll, thereby eliminating the need for expensive equipment and without causing any negative effects on the quality of the strip. It is possible to preheat nine strips using the sensible heat of the combustion exhaust gas.
第1図ないし第3図は本発明法をストリップの連続焼鈍
に適用し大場合の一実施例を示すもので、(2)は加熱
炉、(段は均熱炉、(4)は急冷設備、(5)は再加熱
炉、(6)は過時効炉、(ηは急冷炉であシ、ストリッ
2(S)はこれら設備、′。Figures 1 to 3 show an example in which the method of the present invention is applied to continuous annealing of strips, in which (2) is a heating furnace, (stage is a soaking furnace, and (4) is a rapid cooling equipment. , (5) is a reheating furnace, (6) is an overaging furnace, (η is a quenching furnace, and strip 2 (S) is these facilities, ′.
内を順次連続的に移送きれる。このような設備において
、本発明は、加熱炉(a)さらには再加熱炉(5)入側
の通板ロール(1)をヒートロールとして構成せしめ、
この通板ロール(1)内に加熱炉(2)、再加熱炉(5
)の燃焼排ガスの顕熱を回収した熱媒を流通せしめ、踪
通板ロール(1)を通過するス)9ツブをその顕熱で予
熱するものである。The inside can be transferred sequentially and continuously. In such equipment, the present invention configures the passing roll (1) on the entry side of the heating furnace (a) and further the reheating furnace (5) as a heat roll,
A heating furnace (2) and a reheating furnace (5) are placed inside this threading roll (1).
) A heating medium is circulated through which the sensible heat of the combustion exhaust gas is recovered, and the sensible heat is used to preheat the tubes passing through the passing board roll (1).
上記熱媒として陰部沸点有機熱媒が利用され、このうち
でも主として熱安定性が良好な芳香族類の有−熱媒が利
用される。As the heating medium, an organic heating medium with a negative boiling point is used, and among these, an aromatic heating medium having good thermal stability is mainly used.
熱媒として要求される条件としては高沸点で熱安定性に
優れていることがあげられるが、通常冷媒としての水は
使用限界が高圧下でせいぜい200℃程度であるのに対
し、上記高沸点有機熱媒は400 ’O程度まで熱的に
安定であり、シかも凝固点、腐食性、毒性、防爆性、取
扱いの容易性等においても水とさほど劣らない特性を有
している。The conditions required for a heating medium include a high boiling point and excellent thermal stability.Water, which is normally used as a refrigerant, has a usage limit of about 200°C at most under high pressure, whereas the above-mentioned high boiling point Organic heating media are thermally stable up to about 400'O, and have properties that are not inferior to water in terms of freezing point, corrosivity, toxicity, explosion resistance, ease of handling, etc.
第2図は本発明′11法を模式的に示すもので、(8)
は熱媒O循環管゛絡系、(9)は熱焼排ガスの排出管路
系、輪は熱交換装置であシ、上記循環管路系(8)途中
にヒートロールたる通板ロール(fal) (lb)が
介在している。本実施例で使用される通板ロール(1)
は第3図で示すようにp−ル外l!1l(101)の内
側に接した螺旋状0熱謀流通路(102)を備えたもの
で、本実施例ではストリップ(S)に与える熱量を大き
くするため加熱炉(2)(又は再加熱炉(5))の入側
式2本1組で設けられている。なお、その他図面におい
て、(ハ)はエアセパレータ、(ロ)は膨痕タンク、轡
は循環ポンプ、o4は昇圧ファン、(ト)は煙突である
。そして本発明においては、循環ポンプ(2)によって
熱媒を循環管路系(8)内を循環せしめ、その途中で熱
交換装置(ト)によシ加熱炉(2)(又は再加熱炉(5
))からの燃焼排ガスの顕熱を回′収せしめ、−さらに
かかる熱媒を通板ロール(1a)(1b)内を通過せし
めることにより、該通販ロール(la) (lb)を介
してストリップ(S)に熱を与え予熱を行うものである
。ここで前記加熱炉(2))等から排出される燃焼排ガ
スは通常400°0程度で69、この温度を利用してス
トリップ(8)の有効な予熱を行うことができる。Figure 2 schematically shows the '11 method of the present invention, (8)
(9) is a heating medium O circulation pipe system, (9) is a heat exchange exhaust gas discharge pipe system, and the ring is a heat exchange device. ) (lb) is present. Threading roll (1) used in this example
As shown in FIG. In this embodiment, in order to increase the amount of heat given to the strip (S), it is equipped with a heating furnace (2) (or reheating furnace). (5)) A set of two entry-side type pipes are provided. In addition, in other drawings, (c) is an air separator, (b) is a swelling tank, o4 is a circulation pump, o4 is a booster fan, and (g) is a chimney. In the present invention, the heat medium is circulated in the circulation pipe system (8) by the circulation pump (2), and in the middle of the circulation, it is passed through the heat exchanger (G) to the heating furnace (2) (or reheating furnace). 5
)) by recovering the sensible heat of the flue gas from the combustion exhaust gas, and by passing the heating medium through the plate rolls (1a) and (1b), the strip is passed through the mail order rolls (la) and (lb). (S) is preheated by applying heat. Here, the combustion exhaust gas discharged from the heating furnace (2) etc. is normally at a temperature of about 400° 69, and this temperature can be used to effectively preheat the strip (8).
このような予熱効果は熱媒の顕熱回収率、通、1ja−
ル(1)の本数、ストリップ(S)と通販ロール(1)
との接触面積(巻取角)等の条件によシ異なるが、実験
によれば本実施例のように2本の通販ロール(la)
(lb)を使用してこれに加熱炉(2)の顕熱を回収し
た芳香族類の有機熱媒を通し、板厚1.2−のストリッ
プを7゜t/Hの能力で″処理した場合、70〜10
G ’0の予熱効蕪をあげられることが確認された。Such a preheating effect reduces the sensible heat recovery rate of the heating medium,
Number of rolls (1), strips (S) and mail order rolls (1)
Although it differs depending on conditions such as the contact area (winding angle) with the
A 1.2-thick strip was treated at a capacity of 7°t/H by passing an aromatic organic heating medium from which the sensible heat of the heating furnace (2) had been recovered using a heating furnace (lb). case, 70-10
It was confirmed that the preheating effect of G'0 can be increased.
キして、かかる予熱効果は約15〜20−の燃料節約と
なるものである。第4図は連続焼鈍の熱サイクルを示す
ものであるが、本発明によれば図中斜線で示す部分O熱
負荷を低減せしめることができる。なお、上記したよう
に本発明は通板ロール(1]の数及びこれに対するスト
リップ(S)の接触面積(巻付角)を選択することによ
シ適宜な予熱効果を得ることができる。Thus, such a preheating effect results in a fuel savings of approximately 15-20. FIG. 4 shows a thermal cycle of continuous annealing, and according to the present invention, it is possible to reduce the heat load in the portion O indicated by diagonal lines in the figure. As described above, in the present invention, an appropriate preheating effect can be obtained by selecting the number of threading rolls (1) and the contact area (wrapping angle) of the strip (S) therewith.
また一般に加熱炉においては、高温の炉内通板ロールに
低温(常温)゛のストリップが接触することによp1炉
内温度とストリップ温度との温度差に起因した凹状の熱
クラウンがロールに生じ、ストリップの炉内通板上の障
害となることが知られているが、本発明ではストリップ
を予熱するためこの温度差が小さくなシ、生ずる熱クラ
ウンを小さいものとし、炉内通板性を向上せしめること
ができる。Additionally, in general, in a heating furnace, when a low-temperature (room temperature) strip comes into contact with a high-temperature furnace passing roll, a concave thermal crown is formed on the roll due to the temperature difference between the P1 furnace temperature and the strip temperature. However, in the present invention, since the strip is preheated, this temperature difference is small, and the resulting thermal crown is made small, which improves the ability to pass the strip through the furnace. It can be improved.
実施例1
連続焼鈍設備の加熱炉入側の2本の通板ロールをヒート
ロールとし、これに上記加熱炉の燃焼排ガスの顕熱を回
収した高沸点有機熱媒を流通せしめて予熱を行った。そ
の条件は以下の通りである。Example 1 Two sheet passing rolls on the heating furnace entry side of continuous annealing equipment were used as heat rolls, and a high boiling point organic heating medium that recovered the sensible heat of the combustion exhaust gas of the heating furnace was passed through them to perform preheating. . The conditions are as follows.
ストリップサイズ
板厚:0.8■
幅 : 1000■
ライン速度゛160愼/分
ヒートロー尼2本X1050φ■
ストリップ巻付角:約400°(ロール2本分)この結
果、従来約40′0程度の温度であったものが、約14
0°0に予熱された状態となシ、100℃程度の予熱効
果が得られた。Strip size Thickness: 0.8 ■ Width: 1000 ■ Line speed: 160 centimeters/min 2 heat rolls x 1050 φ ■ Strip winding angle: approx. 400° (for 2 rolls) As a result, the conventional The temperature was about 14
A preheating effect of about 100°C was obtained even when the temperature was preheated to 0°C.
また、この結果、約20参の燃料を節減することができ
た。Additionally, as a result, we were able to save about 20 cents of fuel.
実施例2
連続溶融亜鉛メッキ設備の加熱炉入側の3本の通板ロー
ルをヒートロールとし、上記実施例と同様の方法で予熱
を行った。その条件は以下の通シである。Example 2 Three sheet passing rolls on the heating furnace entry side of continuous hot-dip galvanizing equipment were used as heat rolls, and preheating was performed in the same manner as in the above example. The conditions are as follows.
ストリップサイズ
板厚=1.3■
幅 :117S−
ライン速度:50.7分
ヒートロール:3本X1200φ■
ストリツプ巻付角:約600°(ロール3本分)この結
果、従来約20’O@度の温度でめったものが、約20
0 ’Oに予熱された状態に昌
なj)、180℃程度の予熱効果が得られた。Strip size thickness = 1.3 ■ Width: 117S - Line speed: 50.7 minutes Heat rolls: 3 x 1200φ ■ Strip winding angle: Approx. 600° (for 3 rolls) As a result, conventional approx. 20'O @ Rarely, at a temperature of about 20 degrees
When the temperature was preheated to 0'O, a preheating effect of about 180°C was obtained.
′1、
また、この結果、約sonの燃料を節減することができ
た。'1. Also, as a result, we were able to save about 1 son of fuel.
以上述べた本発明法によれば、大損りな設備を要せずし
て、しかもストリップの品質に悪影響を与えることなく
、加熱炉から排出され九燃焼排ガスの顕熱を有効に利用
してストリップの予熱を行うことができ、加熱炉の燃料
原単位を下げ、経済的且つ適正な熱処理を行うことがで
きるという優れた効果がある。According to the above-described method of the present invention, the sensible heat of the flue gas discharged from the heating furnace is effectively used to produce strips without requiring any major equipment and without adversely affecting the quality of the strips. It has the excellent effect of being able to perform preheating, lowering the fuel consumption rate of the heating furnace, and performing economical and appropriate heat treatment.
第1図ないしs21図は本発明法を連続焼鈍工程に適用
した場合の一実施例を示すもので、M 1図はライン全
体を示す説明図、第2図は本発明法を模式的に示す説明
図、第3図d本発明で用いられる通11ia−ルを概略
的に示す説明図である。第4図は41図に示す連続焼鈍
ラインにおける熱サイクル及びこれに対する本発明によ
る熱負担低減効果を示すものである。
図において、(1) (1m) (lb)は通販ロール
、(2)は加熱炉、(5)は再加熱炉、(8)、はスト
リップを各示す。Figures 1 to s21 show an example in which the method of the present invention is applied to a continuous annealing process, Figure M1 is an explanatory diagram showing the entire line, and Figure 2 schematically shows the method of the present invention. Explanatory drawing, FIG. 3d is an explanatory drawing schematically showing the passageway 11ia used in the present invention. FIG. 4 shows the thermal cycle in the continuous annealing line shown in FIG. 41 and the heat load reducing effect of the present invention on this. In the figure, (1) (1m) (lb) indicates a mail order roll, (2) a heating furnace, (5) a reheating furnace, and (8) a strip.
Claims (1)
通板ロール内に1前記加熱炉の燃焼排ガスの顕熱を熱交
換装置に、よシ回収せしめた高沸点有機熱媒を流通せし
゛め、除通板ロールにてストリ、ツブの予熱を行う9件
を特徴とする連続熱処理設備におけるストリップの予熱
方法。A high boiling point organic heating medium, which has recovered the sensible heat of the combustion exhaust gas of the heating furnace to a heat exchange device, is passed through a passing roll installed on the inlet side of the heating furnace of continuous heat treatment equipment for strip. A method for preheating a strip in a continuous heat treatment facility, which is characterized by nine methods of preheating the strip and the whelk using a removing plate roll.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP17070181A JPS5873727A (en) | 1981-10-27 | 1981-10-27 | Preheating method of strip in continuous heat treatment equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP17070181A JPS5873727A (en) | 1981-10-27 | 1981-10-27 | Preheating method of strip in continuous heat treatment equipment |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5873727A true JPS5873727A (en) | 1983-05-04 |
JPS6241296B2 JPS6241296B2 (en) | 1987-09-02 |
Family
ID=15909788
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP17070181A Granted JPS5873727A (en) | 1981-10-27 | 1981-10-27 | Preheating method of strip in continuous heat treatment equipment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5873727A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6296620A (en) * | 1985-10-24 | 1987-05-06 | Kawasaki Steel Corp | Preheating method and equipment for continuous heat treatment of metal strip |
CN104004898A (en) * | 2014-05-28 | 2014-08-27 | 南京钢铁股份有限公司 | Heating process for sulfuric acid leaking point corrosion resisting band steel |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5741330A (en) * | 1980-08-26 | 1982-03-08 | Nippon Steel Corp | Preheater for steel strip |
-
1981
- 1981-10-27 JP JP17070181A patent/JPS5873727A/en active Granted
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5741330A (en) * | 1980-08-26 | 1982-03-08 | Nippon Steel Corp | Preheater for steel strip |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6296620A (en) * | 1985-10-24 | 1987-05-06 | Kawasaki Steel Corp | Preheating method and equipment for continuous heat treatment of metal strip |
CN104004898A (en) * | 2014-05-28 | 2014-08-27 | 南京钢铁股份有限公司 | Heating process for sulfuric acid leaking point corrosion resisting band steel |
Also Published As
Publication number | Publication date |
---|---|
JPS6241296B2 (en) | 1987-09-02 |
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