JPH059596A - Heat treating device for metallic wire having metallic gloss - Google Patents

Heat treating device for metallic wire having metallic gloss

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Publication number
JPH059596A
JPH059596A JP18537091A JP18537091A JPH059596A JP H059596 A JPH059596 A JP H059596A JP 18537091 A JP18537091 A JP 18537091A JP 18537091 A JP18537091 A JP 18537091A JP H059596 A JPH059596 A JP H059596A
Authority
JP
Japan
Prior art keywords
wire
gas
oxide film
introducing port
inlet
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.)
Pending
Application number
JP18537091A
Other languages
Japanese (ja)
Inventor
Seiji Shimizu
誠二 清水
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.)
Aichi Steel Corp
Original Assignee
Aichi Steel Corp
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 Aichi Steel Corp filed Critical Aichi Steel Corp
Priority to JP18537091A priority Critical patent/JPH059596A/en
Publication of JPH059596A publication Critical patent/JPH059596A/en
Pending legal-status Critical Current

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  • Heat Treatment Of Strip Materials And Filament Materials (AREA)

Abstract

PURPOSE:To provide the heat treating device for a metallic wire having metallic gloss which can shorten the time for heating up and has excellent productivity. CONSTITUTION:This heat treating device of a strand system has a heating furnace 1 and a cooler 2 and heat treats the wire 7 while continuously inserting the wire 7 therebetween. An oxidizing gas introducing port 40 for supplying an oxide film forming gas 4 in the inlet direction F of the wire 7 is disposed near the inlet of the heating furnace 1 and a reducing gas introducing port 60 for introducing a reducing gas 6 is disposed behind this oxidizing gas introducing port 40. An inert gas introducing port 50 for supplying an inert gas 5 may be installed between the oxidizing gas introducing port 40 and the reducing gas introducing port 60.

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,昇温時間の短縮が可能
で,生産性に優れた,金属光沢を有する金属線材の熱処
理装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a heat treatment apparatus for a metal wire rod having a metallic luster, which is capable of shortening a temperature rising time and is excellent in productivity.

【0002】[0002]

【従来技術】線材には,例えばダイス等により皮むきし
た,光輝な金属光沢を有する金属線材がある。該金属線
材は,皮むき線材とも称され,図8,図9に示すごと
く,ストランド式の熱処理装置で焼き入れや焼き戻し処
理を施し,強度,その他の物性を向上させるための熱処
理が行われている。しかしながら,熱処理するに当たっ
ては,600〜1200℃という比較的高温下で連続し
て皮むき線材を加熱するため,該皮むき線材の表面に酸
化被膜が生ずる。そのため,かかる皮むき線材は,光輝
な金属光沢を失うことがある。そこで,従来の熱処理装
置においては,皮むき線材の金属光沢を保持するため,
図8,図9に示すごとく,加熱炉1及び冷却装置2で
は,還元ガス雰囲気下で熱処理を行っている。かかる還
元ガスとしては,例えばH2 ,アンモニア分解ガス(N
2 +H2 )等が用いられる。
2. Description of the Related Art As a wire rod, there is a metal wire rod having a brilliant metallic luster which is peeled off with a die or the like. The metal wire is also referred to as a stripped wire, and as shown in FIGS. 8 and 9, it is subjected to quenching and tempering in a strand-type heat treatment apparatus and heat treatment for improving strength and other physical properties. ing. However, in the heat treatment, since the stripped wire is continuously heated at a relatively high temperature of 600 to 1200 ° C., an oxide film is formed on the surface of the stripped wire. Therefore, such stripped wire may lose its bright metallic luster. Therefore, in the conventional heat treatment device, in order to maintain the metallic luster of the stripped wire,
As shown in FIGS. 8 and 9, in the heating furnace 1 and the cooling device 2, the heat treatment is performed in a reducing gas atmosphere. Examples of such reducing gas include H 2 and ammonia decomposition gas (N
2 + H 2 ) or the like is used.

【0003】なお,上記皮むき線材は,還元ガス雰囲気
下で熱処理を行っても,高温下で長時間加熱されるた
め,必然的に該皮むき線材の表面は,銀白色を呈するよ
うになる。このように,皮むき線材の表面が銀白色を呈
するに至っても,依然として金属光沢を有するため,そ
の外観は許容される範囲内である。上記ストランド式の
熱処理装置は,図8,図9に示すごとく,線材7をその
軸方向に走行させながら,供給パイプ8内で連続的に熱
処理し,その後巻き取りできるよう配設された方式であ
る。
Since the above stripped wire is heated at a high temperature for a long time even if it is heat-treated in a reducing gas atmosphere, the surface of the stripped wire inevitably becomes silvery white. .. In this way, even if the surface of the stripped wire material becomes silver-white, it still has a metallic luster, so that its appearance is within the allowable range. As shown in FIGS. 8 and 9, the strand-type heat treatment apparatus is a system in which the wire 7 is continuously heat-treated in the supply pipe 8 while traveling in its axial direction, and then wound. is there.

【0004】[0004]

【解決しようとする課題】しかしながら,上記従来技術
には,次の問題点がある。即ち,皮むき線材の表面は,
金属光沢を有するため,熱の吸収率が低い。そのため,
皮むき線材は,昇温に長時間を要することになる。その
結果,例えば皮むき線材が1000℃に加熱されるまで
に,約80秒以上という,長時間を要する(図4参
照)。それ故,熱処理の生産性が低下し,線材がコスト
高となる。
However, the above-mentioned conventional technique has the following problems. That is, the surface of the stripped wire is
Since it has metallic luster, its heat absorption rate is low. for that reason,
Stripped wire requires a long time to heat up. As a result, it takes about 80 seconds or more to heat the stripped wire to 1000 ° C. (see FIG. 4). Therefore, the productivity of heat treatment is reduced and the cost of the wire rod increases.

【0005】このような問題点は,皮むき線材の外,後
述するピーリング線材,酸洗線材等の金属線材において
も同様である。本発明は,かかる従来の問題点に鑑みて
なされたもので,昇温時間の短縮が可能で,生産性に優
れた,金属光沢を有する金属線材の熱処理装置を提供し
ようとするものである。
Such a problem also applies to metal wire rods such as peeling wire rods and pickling wire rods, which will be described later, in addition to the peeled wire rods. The present invention has been made in view of the above conventional problems, and an object of the present invention is to provide a heat treatment apparatus for a metal wire rod having a metallic luster, which can shorten the temperature rise time and is excellent in productivity.

【0006】[0006]

【課題の解決手段】本発明は,加熱炉と冷却装置とを有
すると共にこれらの間に複数の線材を連続的に挿入しな
がら該線材を熱処理するストランド式の熱処理装置にお
いて,上記加熱炉の入口近傍には線材の入口方向へ酸化
膜形成ガスを供給するための酸化ガス導入口を配設し,
また該酸化ガス導入口よりも後方には還元ガスを導入す
るための還元ガス導入口を配設してなることを特徴とす
る金属光沢を有する金属線材の熱処理装置にある。本発
明において最も注目すべきことは,上記加熱炉の入口近
傍には,線材の入口方向へ酸化膜形成ガスを供給するた
めの酸化ガス導入口を配設し,該酸化ガス導入口よりも
後方には,還元ガスを導入するための還元ガス導入口を
配設したことである。
According to the present invention, there is provided a strand-type heat treatment apparatus having a heating furnace and a cooling device and heat-treating the plurality of wire rods while continuously inserting the plurality of wire rods between the heating furnace and the cooling device. An oxidizing gas inlet for supplying an oxide film forming gas is provided near the inlet of the wire,
Further, there is provided a heat treatment apparatus for a metal wire having a metallic luster, which is characterized in that a reducing gas introducing port for introducing a reducing gas is provided behind the oxidizing gas introducing port. What is most noticeable in the present invention is that an oxidizing gas inlet for supplying an oxide film forming gas to the inlet of the wire is provided in the vicinity of the inlet of the heating furnace, and the oxidizing gas introducing port is provided behind the oxidizing gas introducing port. In the above, a reducing gas inlet for introducing the reducing gas is provided.

【0007】上記酸化膜形成ガスとしては,例えば空
気,水性ガス(H2 O+H2 ),水蒸気(H2 O)を用
いる。また,上記酸化ガス導入口には,加熱炉におけ
る,各加熱温度の昇温段階に応じて,上記酸化膜形成ガ
スの適正供給ができるよう,例えばバルブによるガス供
給調整装置を配設する(図3)。なお,上記空気は,少
量供給することもできる(図5)。また,上記還元ガス
としては,例えば水素ガス(H2 ),アンモニア分解ガ
ス(N2 +H2 )を用いる。また,上記還元ガス導入口
には,上記酸化ガス導入口と同様に,バルブによるガス
供給調整装置を配設する。
As the oxide film forming gas, for example, air, water gas (H 2 O + H 2 ) or water vapor (H 2 O) is used. In addition, a gas supply adjusting device such as a valve is installed at the oxidizing gas inlet so that the oxide film forming gas can be appropriately supplied according to the heating temperature of each heating temperature in the heating furnace (see FIG. 3). The air can be supplied in a small amount (Fig. 5). Further, as the reducing gas, for example, hydrogen gas (H 2 ) or ammonia decomposition gas (N 2 + H 2 ) is used. In addition, a gas supply adjusting device using a valve is arranged at the reducing gas introducing port, like the oxidizing gas introducing port.

【0008】また,上記酸化ガス導入口と還元ガス導入
口との間には,アルゴンガス(Ar),窒素ガス
(N2 )等の不活性ガスを供給するための不活性ガス導
入口を配設することが好ましい。これにより,上記酸化
膜形成ガスと,上記還元ガスとしての水素ガス(H2
とが混じり合って爆発を生ずることを防止することがで
きる。しかしながら,上記酸化膜形成ガスとして水性ガ
ス(H2 O+H2 )を用いた場合には,上記還元ガスと
しての水素ガス(H2 )と混じり合っても差しつかえな
い。そのため,かかる場合には,不活性ガス導入口を配
設する必要はない(図6)。上記ストランド式の熱処理
装置は,例えば巻回してある金属線材を,一本づつ伸ば
しながら多数本並列して供給できる,線材供給装置を有
する(図2)。
An inert gas inlet for supplying an inert gas such as argon gas (Ar) or nitrogen gas (N 2 ) is provided between the oxidizing gas inlet and the reducing gas inlet. It is preferable to install it. As a result, the oxide film forming gas and the hydrogen gas (H 2 ) as the reducing gas are obtained.
It is possible to prevent the explosion from being generated by mixing with and. However, when water gas (H 2 O + H 2 ) is used as the oxide film forming gas, it may be mixed with hydrogen gas (H 2 ) as the reducing gas. Therefore, in such a case, it is not necessary to provide the inert gas introduction port (Fig. 6). The above-mentioned strand-type heat treatment apparatus has a wire rod supply device that can feed a plurality of wound metal wire rods in parallel while stretching them one by one (FIG. 2).

【0009】また,本発明においては,線材として,例
えばSUS440B,SUS410,SUS304,S
US316,Ti合金からなる金属線材を用いることが
できる。また,これらの金属線材は,酸化膜形成ガスの
雰囲気下で加熱しても良い最高温度が次のごとくであ
る。即ち,例えばSUS440Bは600℃,SUS4
10は390℃,SUS304は500℃,SUS31
6は520,Ti合金は300℃である。
Further, in the present invention, as the wire rod, for example, SUS440B, SUS410, SUS304, S
A metal wire made of US316, Ti alloy can be used. Further, the maximum temperature at which these metal wires may be heated in the atmosphere of the oxide film forming gas is as follows. That is, for example, SUS440B is 600 ° C., SUS4
10 is 390 ℃, SUS304 is 500 ℃, SUS31
6 is 520, and Ti alloy is 300 ° C.

【0010】また,該金属線材は,その軸方向に走行さ
せながら,上記加熱炉,冷却装置,焼き戻し炉ヘ連続し
て供給し,熱処理後に巻き取り装置により巻き取られる
(図1)。また,上記金属光沢を有する金属線材として
は,例えばダイスにより皮むきした皮むき線材,バイト
によりピーリング処理したピーリング線材,引き抜き伸
線材などがある。この引き抜き伸線材としては,酸洗浄
処理をした酸洗線材,皮むき線材,ピーリング線材など
がある。
The metal wire rod is continuously fed to the heating furnace, the cooling device and the tempering furnace while running in the axial direction thereof, and is wound by a winding device after heat treatment (FIG. 1). Examples of the metal wire rod having the metallic luster include a peeled wire rod peeled with a die, a peeled wire rod peeled with a bite, and a drawn wire rod. Examples of the drawn wire rod include an acid-washed wire rod, a peeled wire rod, and a peeling wire rod.

【0011】[0011]

【作用及び効果】本発明においては,上記加熱炉の入口
近傍には,線材の入口方向へ酸化膜形成ガスを供給する
ための酸化ガス導入口が配設してある。そのため,金属
線材が例えば約600℃に加熱されるまでの初期加熱段
階においては,該金属線材は酸化雰囲気下で,加熱され
る。そして,この初期加熱の段階において,該金属線材
の表面に,例えば0.5μm程度の厚みの酸化被膜が生
ずる。このように,酸化被膜が生ずることにより,金属
線材の熱の吸収率が向上する。そのため,金属線材はそ
の後早急に加熱され易くなり,例えば約1000℃まで
の昇温時間の短縮が可能となる(図4)。
In the present invention, an oxidizing gas inlet for supplying an oxide film forming gas toward the inlet of the wire is provided near the inlet of the heating furnace. Therefore, in the initial heating stage until the metal wire is heated to, for example, about 600 ° C., the metal wire is heated in an oxidizing atmosphere. Then, in this initial heating stage, an oxide film having a thickness of, for example, about 0.5 μm is formed on the surface of the metal wire. In this way, the heat absorption rate of the metal wire is improved due to the formation of the oxide film. Therefore, the metal wire is likely to be heated immediately thereafter, and the heating time up to, for example, about 1000 ° C. can be shortened (FIG. 4).

【0012】一方,上記酸化ガス導入口よりも後方に
は,還元ガスを導入するための還元ガス導入口が配設し
てある。そのため,金属線材が例えば600〜1200
℃の比較的高温下で熱処理される中期ないし終期段階に
おいては,上記酸化被膜がそれ以上に増大することがな
い。それ故,金属線材の表面は,例えば約0.5μm程
度の厚みの酸化被膜が生じている程度で,銀白色が保持
されたままの金属光沢を有する状態となる。以上のごと
く,本発明によれば,銀白色の金属光沢が保持されたま
ま,昇温時間の短縮が可能な,生産性に優れた,金属光
沢を有する金属線材の熱処理装置を提供することができ
る。
On the other hand, a reducing gas introducing port for introducing a reducing gas is provided behind the oxidizing gas introducing port. Therefore, the metal wire is, for example, 600 to 1200.
In the middle or final stage of heat treatment at a relatively high temperature of ° C, the oxide film does not grow any further. Therefore, the surface of the metal wire has a metallic luster while retaining silver-white color, for example, to the extent that an oxide film having a thickness of about 0.5 μm is formed. As described above, according to the present invention, it is possible to provide a heat treatment apparatus for a metal wire rod having a metallic luster, which is capable of shortening the temperature rising time while maintaining the silver-white metallic luster and is excellent in productivity. it can.

【0013】[0013]

【実施例】【Example】

実施例1 本発明の実施例にかかる,金属光沢を有する金属線材の
熱処理装置につき,図1〜図6を用いて説明する。即
ち,本例の熱処理装置は,図1,図2に示すごとく,加
熱炉1と冷却装置2とを有すると共に,これらの間に4
本の線材7を連続的に挿入しながら,該線材7を熱処理
するストランド式の装置である。また,上記加熱炉1の
入口近傍11には,線材7の入口方向Fへ酸化膜形成ガ
ス4を供給するための酸化ガス導入口40を配設し,ま
た該酸化ガス導入口40よりも後方には還元ガス6を導
入するための還元ガス導入口60を配設してある。ま
た,冷却装置2の後方には,焼戻し炉3が設けてある。
Example 1 A heat treatment apparatus for a metal wire having metallic luster according to an example of the present invention will be described with reference to FIGS. That is, the heat treatment apparatus of this example has a heating furnace 1 and a cooling apparatus 2 as shown in FIGS.
This is a strand type device that heat-treats the wire rod 7 while continuously inserting the wire rod 7. In addition, an oxidizing gas inlet 40 for supplying the oxide film forming gas 4 in the inlet direction F of the wire 7 is provided in the vicinity 11 of the inlet of the heating furnace 1 and behind the oxidizing gas inlet 40. A reducing gas introducing port 60 for introducing the reducing gas 6 is provided in the. Further, a tempering furnace 3 is provided behind the cooling device 2.

【0014】上記酸化膜形成ガスとしては,図3に示す
ごとく,空気44を用いる。また,上記酸化膜形成ガス
は,図1,図5,図6に示すごとく,酸化ガス導入口4
0を通じて,送風機等を用いて,加熱炉1内に送り込
む。そして,図1,図2に示すごとく,上記酸化膜形成
ガスは,線材7の入口方向Fへ流れるように,加熱炉1
内へ供給する。また,上記酸化ガス導入口40と還元ガ
ス導入口60との間には,図1,図2に示すごとく,不
活性ガス5を導入するための不活性ガス導入口50を配
設する。該不活性ガス5としては,図3に示すごとく,
Arガス55を用いる。
As the oxide film forming gas, air 44 is used as shown in FIG. In addition, the oxide film forming gas is, as shown in FIGS.
Through 0, it is sent into the heating furnace 1 using a blower or the like. As shown in FIGS. 1 and 2, the oxide film forming gas flows in the heating furnace 1 so that it flows in the inlet direction F of the wire 7.
Supply inside. Further, an inert gas inlet 50 for introducing the inert gas 5 is provided between the oxidizing gas inlet 40 and the reducing gas inlet 60 as shown in FIGS. As the inert gas 5, as shown in FIG.
Ar gas 55 is used.

【0015】また,上記酸化ガス導入口40,不活性ガ
ス導入口50,還元ガス導入口60は,上記加熱炉1内
のガス供給パイプ8にそれぞれ連結してある。また,加
熱炉1の後方上部には,還元ガス排出口67を配設す
る。また,上記酸化ガス導入口40,不活性ガス導入口
50,還元ガス導入口60には,図3に示すごとく,昇
温段階(常温〜1200℃)に応じて,上記酸化膜形成
ガス4,不活性ガス5,還元ガス6の適正供給ができる
よう,多数のバルブ41〜43,51〜53,61〜6
5を用いた供給調整装置が配設してある。これにより,
線材7の種類,成分に対応した,加熱温度と,酸化,還
元,不活性ガス雰囲気を提供することができる。
The oxidizing gas inlet 40, the inert gas inlet 50, and the reducing gas inlet 60 are connected to the gas supply pipe 8 in the heating furnace 1, respectively. Further, a reducing gas discharge port 67 is provided in the upper rear part of the heating furnace 1. In addition, as shown in FIG. 3, the oxidizing gas inlet 40, the inert gas inlet 50, and the reducing gas inlet 60 are connected to the oxide film forming gas 4 and the oxide film forming gas 4 according to the temperature raising step (normal temperature to 1200 ° C.). A large number of valves 41 to 43, 51 to 53, 61 to 6 so that the inert gas 5 and the reducing gas 6 can be appropriately supplied.
A supply adjusting device using No. 5 is provided. By this,
It is possible to provide a heating temperature and an oxidizing, reducing, or inert gas atmosphere corresponding to the type and composition of the wire 7.

【0016】また,図5に示すごとく,少量の空気44
を用いることもできる。更に,図6に示すごとく,水性
ガス(H2 O+H2 )45を用いることができる。な
お,図6に示すごとく,酸化膜形成ガスとして水性ガス
45を用いた場合には,上記不活性ガス導入口は配設し
ない。酸化膜形成ガスと還元ガスとが混合しても燃焼,
爆発を生じないからである。また,上記線材7として
は,皮むき線材を用いる。該皮むき線材は,例えば1〜
5mm径のものを,4本並列した状態で,走行させるよ
う,線材供給装置より上記加熱炉1内へ連続して送り込
まれる。また,上記加熱炉1の後方には,図1,図2に
示すごとく,冷却装置2及び焼戻炉3を配設する。該冷
却装置2には,図2に示すごとく,水冷パイプ21が配
管してある。また,上記焼戻炉3は,炉内が約400〜
700℃の雰囲気になるように構成してある。
Further, as shown in FIG. 5, a small amount of air 44
Can also be used. Further, as shown in FIG. 6, water gas (H 2 O + H 2 ) 45 can be used. Note that, as shown in FIG. 6, when the water gas 45 is used as the oxide film forming gas, the above inert gas inlet is not provided. Combustion even if the oxide film forming gas and the reducing gas are mixed,
This is because no explosion will occur. A stripped wire is used as the wire 7. The stripped wire is, for example, 1 to
Four wire rods having a diameter of 5 mm are continuously fed from the wire rod feeding device into the heating furnace 1 so that they run in parallel. A cooling device 2 and a tempering furnace 3 are provided behind the heating furnace 1 as shown in FIGS. As shown in FIG. 2, the cooling device 2 is provided with a water cooling pipe 21. In addition, the tempering furnace 3 has about 400-
The atmosphere is set to 700 ° C.

【0017】また,上記焼戻炉3の後方には,熱処理を
終了した線材7を連続的に巻き取るための線材巻取り装
置9が配置してある。その他は,従来のストランド式の
熱処理装置と同様である。本例においては,上記加熱炉
1の入口近傍11には,図1,図2に示すごとく,線材
7の入口方向Fへ酸化膜形成ガス4を供給するための酸
化ガス導入口40が配設してある。そのため,線材7と
してSUS440Bを用いた場合には,約600℃に加
熱されるまでの熱処理の初期段階において,該線材7は
酸化雰囲気下で加熱される。そして,この初期段階にお
いて,該線材7の表面に,厚みが約0.5μmの酸化被
膜が生ずる。
Further, behind the tempering furnace 3, there is arranged a wire rod winding device 9 for continuously winding the heat-treated wire rod 7. Others are the same as the conventional strand type heat treatment apparatus. In the present example, an oxidizing gas inlet 40 for supplying the oxide film forming gas 4 in the inlet direction F of the wire 7 is provided near the inlet 11 of the heating furnace 1 as shown in FIGS. I am doing it. Therefore, when SUS440B is used as the wire 7, the wire 7 is heated in an oxidizing atmosphere in the initial stage of the heat treatment until it is heated to about 600 ° C. Then, in this initial stage, an oxide film having a thickness of about 0.5 μm is formed on the surface of the wire 7.

【0018】このように,酸化被膜が生ずることによ
り,線材7の熱の吸収率が向上する。そのため,線材7
はその後早急に加熱され易くなり,例えば,約1000
℃までの昇温時間の短縮が可能となる。即ち,図4に示
すごとく,本発明(曲線A)においては,線材7を約1
000℃までに加熱するための経過時間は,約40秒間
の比較的短時間であった。これに対して,最初から還元
ガス雰囲気のみで加熱する従来例(曲線B)において
は,1000℃までの加熱に約80秒間を要していたの
で,昇温時間が半分に短縮ができたことになる。なお,
上記図4は,線材の加熱温度(℃)と経過時間(分)と
の関係を表すグラフであり,線材7としてはSUS44
0Bを用いている。また,線径は2.34mm,雰囲気
温度は1000℃,線材速度は1.2m/分,加熱炉の
長さは4mである。
By thus forming the oxide film, the heat absorption rate of the wire 7 is improved. Therefore, wire 7
Is easily heated soon after, for example, about 1000
It is possible to shorten the heating time up to ° C. That is, as shown in FIG. 4, in the present invention (curve A), about 1
The elapsed time for heating to 000 ° C was a relatively short time of about 40 seconds. On the other hand, in the conventional example (curve B) in which only the reducing gas atmosphere is heated from the beginning, it took about 80 seconds to heat up to 1000 ° C., so the temperature rising time could be reduced to half. become. In addition,
FIG. 4 is a graph showing the relationship between the heating temperature (° C.) of the wire rod and the elapsed time (minutes).
0B is used. The wire diameter is 2.34 mm, the ambient temperature is 1000 ° C., the wire speed is 1.2 m / min, and the length of the heating furnace is 4 m.

【0019】一方,上記酸化ガス導入口40よりも後方
には,不活性ガス導入口50及び還元ガス導入口60が
配設してある。そのため,線材7が例えば1000〜1
200℃に熱処理される終期段階においては,上記酸化
被膜は還元される。それ故,線材1の表面は,銀白色を
有する状態となる。こうして,約1000℃までの昇温
時間の短縮(半減化)が可能となったことになる。それ
故,熱処理の生産性が向上する。
On the other hand, an inert gas inlet 50 and a reducing gas inlet 60 are provided behind the oxidizing gas inlet 40. Therefore, the wire rod 7 is, for example, 1000 to 1.
At the final stage of heat treatment at 200 ° C., the oxide film is reduced. Therefore, the surface of the wire 1 has a silver white color. In this way, the heating time up to about 1000 ° C can be shortened (halved). Therefore, the productivity of heat treatment is improved.

【0020】実施例2 本例は,図7に示すごとく,線材加熱温度(℃)と酸化
被膜生成量との関係を示すものである。即ち,本例にお
いては,線径20mmのSUS440Bを用い,500
℃から900℃の各空気雰囲気温度において,それぞれ
30分間(曲線C)又は60分間(曲線D)加熱した。
そして,線材表面に生成された酸化膜の重量(mg/d
2 )を測定した。その結果を各温度について,図7に
プロットした。同図より知られるごとく,加熱保持を6
0分間行った場合の方がこれより短時間(30分)の場
合よりも,多量の酸化膜が形成される。
Example 2 As shown in FIG. 7, this example shows the relationship between the wire heating temperature (° C.) and the amount of oxide film formed. That is, in this example, SUS440B having a wire diameter of 20 mm was used, and
Heating was carried out for 30 minutes (curve C) or 60 minutes (curve D) at each air atmosphere temperature of ℃ to 900 ℃.
The weight of the oxide film formed on the surface of the wire (mg / d
m 2 ) was measured. The results are plotted in FIG. 7 for each temperature. As can be seen from the figure, the heating hold is 6
A larger amount of oxide film is formed in the case of 0 minute than in the case of shorter time (30 minutes).

【0021】また,ここに重要なことは,空気雰囲気加
熱であっても、600℃まで位は,酸化膜の形成が少な
く,その高温では急速に酸化膜形成量が増大することで
ある。このことからも知られるごとく,SUS440B
においては,600℃まで位は酸化雰囲気中で初期加熱
を行い,酸化膜形成が増大する高温では還元ガス雰囲気
で加熱すると良いことが分かる。なお,初期加熱的に形
成された酸化被膜は高温還元雰囲気中で還元される。ま
た,酸化雰囲気中で加熱する上限温度は,前記に例示し
たごとくそれぞれ異なり,図7に示したごとき実験によ
り定められる。
What is important here is that even when heated in an air atmosphere, the oxide film formation is small up to about 600 ° C., and the oxide film formation amount rapidly increases at the high temperature. As is known from this, SUS440B
It can be seen that in (1), initial heating is performed in an oxidizing atmosphere up to 600 ° C., and heating is performed in a reducing gas atmosphere at a high temperature at which oxide film formation increases. The oxide film formed by initial heating is reduced in a high temperature reducing atmosphere. Further, the upper limit temperature for heating in the oxidizing atmosphere is different as described above, and is determined by the experiment as shown in FIG.

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

【図1】実施例にかかる熱処理装置の側面図。FIG. 1 is a side view of a heat treatment apparatus according to an embodiment.

【図2】実施例にかかる熱処理装置の平面図。FIG. 2 is a plan view of the heat treatment apparatus according to the embodiment.

【図3】実施例における,ガス供給調整装置の取付状態
を示す説明図。
FIG. 3 is an explanatory view showing a mounting state of the gas supply adjusting device in the embodiment.

【図4】線材の加熱された温度と経過時間との関係を示
すグラフ。
FIG. 4 is a graph showing the relationship between the heating temperature of the wire and the elapsed time.

【図5】実施例における,酸化膜形成ガスと不活性ガス
との他の供給状態を示す説明図。
FIG. 5 is an explanatory diagram showing another supply state of the oxide film forming gas and the inert gas in the example.

【図6】実施例1における,酸化膜形成ガスと還元ガス
との他の供給状態を示す説明図。
FIG. 6 is an explanatory view showing another supply state of the oxide film forming gas and the reducing gas in the first embodiment.

【図7】実施例2における,線材加熱時間と酸化被膜の
生成重量との関係を示すグラフ。
FIG. 7 is a graph showing the relationship between the wire heating time and the weight of oxide film produced in Example 2.

【図8】従来の熱処理装置の平面図。FIG. 8 is a plan view of a conventional heat treatment apparatus.

【図9】従来の熱処理装置の側面図。FIG. 9 is a side view of a conventional heat treatment apparatus.

【符号の説明】[Explanation of symbols]

1...加熱炉, 2...冷却装置, 3...焼戻炉, 4...酸化膜形成ガス, 5...不活性ガス, 6...還元ガス, 7...線材, 8...ガス供給パイプ, A...本発明, B...従来例, 1. . . Heating furnace, 2. . . Cooling device, 3. . . Tempering furnace, 4. . . Oxide film forming gas, 5. . . Inert gas, 6. . . Reducing gas, 7. . . Wire rod, 8. . . Gas supply pipe, A. . . The present invention, B. . . Conventional example,

Claims (1)

【特許請求の範囲】 【請求項1】 加熱炉と冷却装置とを有すると共にこれ
らの間に複数の線材を連続的に挿入しながら該線材を熱
処理するストランド式の熱処理装置において,上記加熱
炉の入口近傍には線材の入口方向へ酸化膜形成ガスを供
給するための酸化ガス導入口を配設し,また該酸化ガス
導入口よりも後方には還元ガスを導入するための還元ガ
ス導入口を配設してなることを特徴とする金属光沢を有
する金属線材の熱処理装置。
Claims: What is claimed is: 1. A strand-type heat treatment apparatus having a heating furnace and a cooling device, wherein a plurality of wire rods are continuously inserted between them to heat-treat the wire rods. An oxidizing gas introducing port for supplying an oxide film forming gas toward the inlet of the wire is arranged near the inlet, and a reducing gas introducing port for introducing a reducing gas is provided behind the oxidizing gas introducing port. A heat treatment device for a metal wire rod having a metallic luster, which is characterized by being arranged.
JP18537091A 1991-06-28 1991-06-28 Heat treating device for metallic wire having metallic gloss Pending JPH059596A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18537091A JPH059596A (en) 1991-06-28 1991-06-28 Heat treating device for metallic wire having metallic gloss

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18537091A JPH059596A (en) 1991-06-28 1991-06-28 Heat treating device for metallic wire having metallic gloss

Publications (1)

Publication Number Publication Date
JPH059596A true JPH059596A (en) 1993-01-19

Family

ID=16169615

Family Applications (1)

Application Number Title Priority Date Filing Date
JP18537091A Pending JPH059596A (en) 1991-06-28 1991-06-28 Heat treating device for metallic wire having metallic gloss

Country Status (1)

Country Link
JP (1) JPH059596A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000345243A (en) * 1999-06-07 2000-12-12 Bridgestone Corp Method for uniformly heating plural metallic wire rods and heating furnace
JP2012144803A (en) * 2010-12-24 2012-08-02 Hitachi Metals Ltd Heat treatment apparatus for metal wire rod
JP2013044042A (en) * 2011-08-26 2013-03-04 Hitachi Metals Ltd Heat treatment apparatus for metal wire rod

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000345243A (en) * 1999-06-07 2000-12-12 Bridgestone Corp Method for uniformly heating plural metallic wire rods and heating furnace
JP2012144803A (en) * 2010-12-24 2012-08-02 Hitachi Metals Ltd Heat treatment apparatus for metal wire rod
JP2013044042A (en) * 2011-08-26 2013-03-04 Hitachi Metals Ltd Heat treatment apparatus for metal wire rod

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