JPS5929643B2 - Continuous atmosphere heat treatment furnace - Google Patents
Continuous atmosphere heat treatment furnaceInfo
- Publication number
- JPS5929643B2 JPS5929643B2 JP50111071A JP11107175A JPS5929643B2 JP S5929643 B2 JPS5929643 B2 JP S5929643B2 JP 50111071 A JP50111071 A JP 50111071A JP 11107175 A JP11107175 A JP 11107175A JP S5929643 B2 JPS5929643 B2 JP S5929643B2
- Authority
- JP
- Japan
- Prior art keywords
- heated
- chamber
- oxidizing gas
- heat treatment
- objects
- 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
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
- C21D1/00—General methods or devices for heat treatment, e.g. annealing, hardening, quenching or tempering
- C21D1/74—Methods of treatment in inert gas, controlled atmosphere, vacuum or pulverulent material
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27B—FURNACES, KILNS, OVENS OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
- F27B9/00—Furnaces through which the charge is moved mechanically, e.g. of tunnel type; Similar furnaces in which the charge moves by gravity
- F27B9/14—Furnaces through which the charge is moved mechanically, e.g. of tunnel type; Similar furnaces in which the charge moves by gravity characterised by the path of the charge during treatment; characterised by the means by which the charge is moved during treatment
- F27B9/20—Furnaces through which the charge is moved mechanically, e.g. of tunnel type; Similar furnaces in which the charge moves by gravity characterised by the path of the charge during treatment; characterised by the means by which the charge is moved during treatment the charge moving in a substantially straight path
- F27B9/24—Furnaces through which the charge is moved mechanically, e.g. of tunnel type; Similar furnaces in which the charge moves by gravity characterised by the path of the charge during treatment; characterised by the means by which the charge is moved during treatment the charge moving in a substantially straight path being carried by a conveyor
- F27B9/2407—Furnaces through which the charge is moved mechanically, e.g. of tunnel type; Similar furnaces in which the charge moves by gravity characterised by the path of the charge during treatment; characterised by the means by which the charge is moved during treatment the charge moving in a substantially straight path being carried by a conveyor the conveyor being constituted by rollers (roller hearth furnace)
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
- F27D99/00—Subject matter not provided for in other groups of this subclass
- F27D99/0073—Seals
- F27D99/0075—Gas curtain seals
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 Articles (AREA)
- Heat Treatments In General, Especially Conveying And Cooling (AREA)
Description
【発明の詳細な説明】
本発明はパイプ又は棒状材等の長尺被熱物を不活性ガス
或いは還元性ガス(以下無酸化性ガスという)雰囲気中
で連続的に無酸化焼鈍或いは光輝焼鈍する熱処理方法に
関するものである。[Detailed description of the invention] The present invention continuously performs non-oxidation annealing or bright annealing of a long object to be heated, such as a pipe or a rod-shaped material, in an inert gas or reducing gas (hereinafter referred to as non-oxidizing gas) atmosphere. The present invention relates to a heat treatment method.
第1図は従来の連続雰囲気熱処理炉の一例を示す。FIG. 1 shows an example of a conventional continuous atmosphere heat treatment furnace.
図において、1は装入テーブル、2は入口扉、3は前室
、4は加熱室、5は均熱室、6は電気抵抗発熱体、7は
冷却室、8は後室、9は出口扉、10は抽出テーブル、
11は搬送ロール、12は前室内の天井部より吊下され
た耐熱繊維よりなる防風カーテン、13は後室内の天井
部より吊下された耐熱繊維よりなる防風カーテン、14
は装入テーブル1の上部に設けられた排ガス集合排出装
置である。In the figure, 1 is a charging table, 2 is an entrance door, 3 is a front chamber, 4 is a heating chamber, 5 is a soaking chamber, 6 is an electric resistance heating element, 7 is a cooling chamber, 8 is a rear chamber, and 9 is an outlet Door, 10 is extraction table,
11 is a transport roll; 12 is a windproof curtain made of heat-resistant fibers suspended from the ceiling in the front room; 13 is a windbreak curtain made of heat-resistant fibers suspended from the ceiling in the rear room; 14
is an exhaust gas collection and discharge device provided above the charging table 1.
加熱室4、均熱室5及び冷却室7には無酸化性ガスが図
示しないガス発生装置から管15を通して供給されて加
熱室4、均熱室5及び冷却室7内をこの雰囲気ガスによ
って充満させている。A non-oxidizing gas is supplied to the heating chamber 4, soaking chamber 5, and cooling chamber 7 from a gas generator (not shown) through a pipe 15, and the heating chamber 4, soaking chamber 5, and cooling chamber 7 are filled with this atmospheric gas. I'm letting you do it.
被熱物aは搬送ロール110回転によって前室3、加熱
室4、均熱室5、冷却室7の順に搬送されるが、被熱物
aがパイプ又は棒状材のような長尺物の場合、加熱室4
に搬入されるときにパイプの内部或いは数本積み重なっ
た棒状材の隙間等の長尺空間には熱気が容易には流入し
ないので均一加熱を図るには長時間を要する欠点があっ
た。The object to be heated a is conveyed in the order of the front chamber 3, the heating chamber 4, the soaking chamber 5, and the cooling chamber 7 by 110 rotations of the conveyor roll, but when the object to be heated is a long object such as a pipe or a rod-shaped material, , heating chamber 4
Since hot air does not easily flow into a long space such as the inside of a pipe or the gap between several stacked rods when it is transported into a warehouse, it has the disadvantage that it takes a long time to achieve uniform heating.
また、冷却の場合にも同様に長尺被熱物の場合能率が極
めて悪く、これに対し従来では、処理能力を高めんとす
れば炉長を長くするほかなかったので設備費が高(なる
欠点を有していた。In addition, in the case of cooling, the efficiency is also extremely low in the case of long objects to be heated.In contrast, in the past, the only way to increase the processing capacity was to increase the length of the furnace, which resulted in high equipment costs. It had drawbacks.
本発明は上記欠点を解消した長尺被熱物の連続雰囲気熱
処理方法を提供せんとするものである。The present invention aims to provide a continuous atmosphere heat treatment method for long objects to be heated, which eliminates the above-mentioned drawbacks.
次に本発明の一実施例を第4図乃至第8図に従い説明す
る。Next, one embodiment of the present invention will be described with reference to FIGS. 4 to 8.
この第4図乃至第8図に使用した符号は前に説明した第
1図乃至第3図と同一符号は同一部分を示すものとして
その説明を省略する。The same reference numerals used in FIGS. 4 to 8 as those in FIGS. 1 to 3 described above indicate the same parts, and the explanation thereof will be omitted.
16,17は前室3の天井部と底部に夫々設けられたプ
レナムチャンバで、底部のプレナムチャンバ17から般
送ロール11の間隔に被熱物aの進行方向と反対向(第
5図左方向)に傾斜した数本の短筒状のノズル19を突
出させると共に、天井部のプレナムチャンバ16からは
このノズル19と対称位置に相対向する短筒状のノズル
18を同方向に傾斜させて突出させ、プレナムチャンバ
16,17に夫々給気管20.21を介して無酸化性ガ
スを供給する。Reference numerals 16 and 17 indicate plenum chambers provided at the ceiling and the bottom of the front chamber 3, respectively. ), several short cylindrical nozzles 19 are protruded from the plenum chamber 16 on the ceiling, and short cylindrical nozzles 18 are slanted in the same direction and protrude from the plenum chamber 16 at a symmetrical position to the nozzles 19. and supply non-oxidizing gas to the plenum chambers 16 and 17 via air supply pipes 20 and 21, respectively.
そしてノズル18.19の先端から常温の無酸化性ガス
を被熱物a、a・・・・・・に対して斜めに噴射する。Then, non-oxidizing gas at room temperature is injected obliquely from the tips of the nozzles 18 and 19 onto the objects to be heated a, a, . . . .
各被熱物a、a・・・・・・はその長手方向を進行方向
と平行にして前室3に搬入されるが、後続する被熱物と
の間に適宜間隔gを置いて搬入する。Each object to be heated a, a... is carried into the front chamber 3 with its longitudinal direction parallel to the direction of movement, and is carried in with an appropriate distance g between it and the following object to be heated. .
このため第5図の矢印で示すように間隔gにおいてその
上下部の無酸化性ガスが衝突し被熱物aの開口端から無
酸化性ガスがパイプ内部に流入しパイプ内部の空気をこ
の無酸化性ガスの動圧により追い出す。Therefore, as shown by the arrow in Fig. 5, the non-oxidizing gas in the upper and lower portions collides at the interval g, and the non-oxidizing gas flows into the pipe from the open end of the object to be heated, and the air inside the pipe is absorbed by the non-oxidizing gas. It is expelled by the dynamic pressure of oxidizing gas.
従ってこの上下に夫々数本設けられたノズル1B、19
から被熱物a、a・・・・・・の表面に噴出するガスカ
ーテンにより炉内雰囲気ガスを完全に外部と遮断すると
同時に、パイプの先端から内部に圧送されるガスにより
残留せる空気を外部に追い出して加熱炉4内には酸化性
の空気を持ち込まない。Therefore, several nozzles 1B and 19 are provided above and below.
At the same time, the atmosphere gas inside the furnace is completely shut off from the outside by the gas curtain that is ejected from the surface of the heated objects a, a, etc., and at the same time, the remaining air is removed from the outside by the gas that is forced into the inside from the tip of the pipe. This prevents oxidizing air from being brought into the heating furnace 4.
又、本発明では、加熱室4の天井部と底部にプレナムチ
ャンバ22.23を対設し、被熱物a。Furthermore, in the present invention, plenum chambers 22 and 23 are provided oppositely at the ceiling and bottom of the heating chamber 4, and the object to be heated a.
a・・・・・・と対向する面に通気孔24,25を夫々
多数開設すると共に底部のプレナムチャンバ23から搬
送ロール110間隔に被熱物の進行方向と反対方向に傾
斜した数本の短筒状のノズル27を突出させ、天井部の
プレナムチャンバ22からはこのノズル27と対称位置
に相対向する短筒状のノズル26を同方向に傾斜させて
突出させる。A... A large number of ventilation holes 24 and 25 are provided on the surface facing the plenum chamber 23 at the bottom, and several short strips are provided at intervals between the conveyor rolls 110 and are inclined in the direction opposite to the direction of movement of the heated object. A cylindrical nozzle 27 is made to protrude, and a short cylindrical nozzle 26 that faces symmetrically with this nozzle 27 is made to protrude from the plenum chamber 22 on the ceiling while being inclined in the same direction.
プレナムチャンバ22.23は第8図に示したように電
熱ヒーター若しくは燃焼式バーナ等の発熱部28を通過
して高温に加熱された無酸化性ガスがファン29の回転
によって吸引され該無酸化性ガスが分岐管30により圧
送されるので通気孔24゜25及びノズル26,27か
ら被熱物a、a・・・・・・に対して高温度の無酸化性
ガスが噴射される。As shown in FIG. 8, in the plenum chambers 22 and 23, non-oxidizing gas heated to a high temperature after passing through a heat generating part 28 such as an electric heater or a combustion burner is sucked in by the rotation of a fan 29, and the non-oxidizing gas is sucked in by the rotation of a fan 29. Since the gas is fed under pressure through the branch pipe 30, high-temperature non-oxidizing gas is injected from the ventilation holes 24, 25 and nozzles 26, 27 onto the objects a, a, . . . .
このためノズル26.27から噴射したガスは被熱物a
、a・・・・・・の間隔gにおいて衝突することにより
第7図に示されるように被熱物a、a・・・・・・の長
手方向に沿う動圧を生じてパイプ内部に流入し被熱物a
、a・・・・・・を内面より加熱する。Therefore, the gas injected from the nozzles 26 and 27 is
By colliding at intervals g between heated objects a, a..., as shown in Fig. 7, dynamic pressure is generated along the longitudinal direction of the heated objects a, a... and flows into the pipe. heated object a
, a... are heated from the inside.
加熱室4には給気管31から常時無酸化性ガスが補給さ
れておりこのガスがファン290回転によってプレナム
チャンバ22,23に圧送され再び加熱室4内に循環す
るものである。The heating chamber 4 is constantly supplied with non-oxidizing gas from the air supply pipe 31, and this gas is force-fed to the plenum chambers 22, 23 by a fan 290 rotations and circulated back into the heating chamber 4.
従って加熱室4を通過することによって被熱物a、a・
・・・・は内面及び外面から同時に熱を吸収し急速に温
度が上昇する。Therefore, by passing through the heating chamber 4, the heated objects a, a.
... absorbs heat from the inner and outer surfaces at the same time and the temperature rises rapidly.
均熱室5にはプレナムチャンバ32.33が加熱室4で
加熱された被熱物a、a・・・・・・を挟む如く上下部
に対設されており、被熱物a、a・・・・・・と対向す
る面に開設された多数の通気孔から高温度の無酸化性ガ
スを噴射するため被熱物a、a・・・・・・を所定温度
に保持する。In the soaking chamber 5, plenum chambers 32 and 33 are provided at the upper and lower sides of the heated objects a, a, . . . , which are heated in the heating chamber 4. . . . The objects to be heated a, a .
図ポしないがプレナムチャンバ32.33から噴射され
た無酸化性ガスはファンによって吸引され加熱されて再
度プレナムチャンバ32,33に循環する。Although not shown, the non-oxidizing gas injected from the plenum chambers 32, 33 is sucked in by the fan, heated, and circulated to the plenum chambers 32, 33 again.
そして給気管34から均熱室5内に常時無酸化性ガスが
補給されている。Non-oxidizing gas is constantly supplied into the soaking chamber 5 from the air supply pipe 34.
又、冷却室7の天井部と底部には低温度に冷却された無
酸化性ガスを噴出するプレナムチャンバ35.36が対
設されて、被熱物a、a・・・・・・と対向する面に通
気孔を夫々多数開設すると共に底部のプレナムチャンバ
36には被熱物a、a・・・・・・の進行方向に傾斜し
た短筒状のノズル38及びその反対方向に傾斜した短筒
状のノズル40を夫々搬送ロール110間隔に突出させ
、天井部のプレナムチャンバ35からはこれらノズル3
8.40と同方向に傾斜した相対向する短筒状のノズル
37゜39を対称位置に突出させる。In addition, plenum chambers 35 and 36 that eject non-oxidizing gas cooled to a low temperature are provided on the ceiling and bottom of the cooling chamber 7, and are arranged opposite to the objects to be heated a, a, and so on. In addition, the plenum chamber 36 at the bottom has a short cylindrical nozzle 38 inclined in the direction of movement of the heated objects a, a, and so on, and a short cylindrical nozzle 38 inclined in the opposite direction. Cylindrical nozzles 40 are made to protrude at intervals between transport rolls 110, and these nozzles 3 are projected from the plenum chamber 35 in the ceiling.
8. Protrude opposite short cylindrical nozzles 37°39 inclined in the same direction as 40 to symmetrical positions.
これらのノズル群から噴射した無酸化性ガスは加熱室の
場合と同様に被熱物a、a・・・・・・の間隔gにおい
て衝突することにより被熱物a、a・・・・・・の長手
方向に沿う動圧が生じてパイプ内部に流入し被熱物a、
a・・・・・・を内面からも冷却する。As in the case of the heating chamber, the non-oxidizing gas injected from these nozzle groups collides with the objects to be heated a, a,... at the interval g, thereby causing the objects to be heated, a, a...・Dynamic pressure is generated along the longitudinal direction and flows into the pipe, causing the heated object a,
a... is also cooled from the inside.
冷却室7には給気管41によって無酸化性ガスが補給さ
れ、その無酸化性ガスは図示しない水冷熱交換器を通し
て冷却されファンによってプレナムチャンバ35,36
に圧送されて冷却室7内に噴出する。The cooling chamber 7 is supplied with non-oxidizing gas through an air supply pipe 41, and the non-oxidizing gas is cooled through a water-cooled heat exchanger (not shown) and sent to the plenum chambers 35, 36 by a fan.
It is pumped into the cooling chamber 7 and ejected into the cooling chamber 7.
これによって被熱物a、a・・・・・・は内面及び外面
から同時に熱を奪われ大気中で酸化しない程度に温度が
下がる。As a result, the heat objects a, a, .
本発明の連続雰囲気熱処理方法は以上実施例について説
明したようにパイプ或いは棒状材のような長尺被熱物に
おいてパイプ内或いは棒状材の隙間に傾斜したノズルか
ら無酸化性ガスを噴射するため、被熱物は内面及び外面
から急速にその無酸化性ガスの温度に加熱或いは冷却さ
れて熱伝達に時間を要さないので小型ながらも大量の被
熱物を処理出来て極めて高能率の稼動が達成出来る効果
を有するものである。As explained in the embodiments above, the continuous atmosphere heat treatment method of the present invention injects non-oxidizing gas from an inclined nozzle into the inside of the pipe or into the gap between the rods in a long object to be heated such as a pipe or rod. The object to be heated is rapidly heated or cooled to the temperature of the non-oxidizing gas from the inner and outer surfaces, and no time is required for heat transfer, so even though it is small, it can process a large amount of object to be heated and has extremely high efficiency operation. It has the effect that can be achieved.
第1図は従来の連続雰囲気熱処理炉を示す縦断面図、第
2図は第1図のA−A線断面拡大矢視図、第3図は第1
図のB−B線断面拡大矢視図である。
第4図は本発明に係る連続雰囲気熱処理方法の一実施例
を示す炉体の縦断面図、第5図は第4図における前室の
拡大図、第6図はそのC−C線断面矢視図、第7図は第
4図における加熱室の拡大図、第8図はそのD−D線断
面矢視図である。
a、a・・・・・・被熱物、3・・・・・・前室、4・
・・・・・加熱室、5・・・・・・均熱室、7・・・・
・・冷却室、16,17・・・・・・ブレナムチャンバ
、18,19・・・・・ノズル、22゜23・・・・・
・ブレナムチャンバ、26,27・・・・・・ノズル、
28・・・・・・発熱部、29・・・・・・ファン、3
2゜33・・・・・・ブレナムチャンバ、35,36・
・・・・・ブレナムチャンバ、37,3B、39,40
・・・・・・ノズル。Fig. 1 is a vertical cross-sectional view showing a conventional continuous atmosphere heat treatment furnace, Fig. 2 is an enlarged cross-sectional view taken along line A-A in Fig. 1, and Fig. 3 is a vertical cross-sectional view showing a conventional continuous atmosphere heat treatment furnace.
FIG. 3 is an enlarged cross-sectional view taken along line B-B in the figure. FIG. 4 is a longitudinal sectional view of a furnace body showing an embodiment of the continuous atmosphere heat treatment method according to the present invention, FIG. 5 is an enlarged view of the front chamber in FIG. 4, and FIG. 7 is an enlarged view of the heating chamber in FIG. 4, and FIG. 8 is a sectional view taken along line D--D. a, a... Heated object, 3... Front chamber, 4.
... Heating chamber, 5 ... Soaking room, 7 ...
...Cooling chamber, 16,17...Blenheim chamber, 18,19...Nozzle, 22゜23...
・Blenheim chamber, 26, 27... nozzle,
28... Heat generating part, 29... Fan, 3
2゜33...Blenheim chamber, 35,36.
...Blenheim Chamber, 37, 3B, 39, 40
······nozzle.
Claims (1)
を進行方向と平行にして搬送ロール上に支持させ加熱室
から冷却室へ搬送するようになした雰囲気熱処理炉にお
いて、加熱室及び冷却室の底部と天井部に夫々プレナム
チャンバを設け、底部のプレナムチャンバから前記搬送
ロールの間隔に被熱物の進行方向又はその反対方向に傾
斜した数本の短筒状のノズルを突出させると共に、天井
部のプレナムチャンバからは前記ノズルと対称位置に相
対向する短筒状のノズルを同方向に傾斜させて突出させ
、被熱物を加熱室及び冷却室へ搬入する際に後続する被
熱物との間に適宜間隔を置いて搬入し、前記両プレナム
チャンバからノズルを通して噴射された高温度の加熱用
無酸化性ガス及び低温度の冷却用無酸化性ガスを夫々前
記被熱物の間隔において衝突させることにより被熱物の
長手方向に沿う動圧を生じさせて被熱物のパイプ内部又
は棒状材間隙に該各無酸化性ガスが流入するようにした
パイプ又は棒状材等の長尺被熱物の連続雰囲気熱処理方
法。1. In an atmospheric heat treatment furnace in which a long object to be heated, such as a pipe or a rod-shaped material, is supported on a conveyor roll with its longitudinal direction parallel to the direction of movement and conveyed from the heating chamber to the cooling chamber, the heating chamber and A plenum chamber is provided at the bottom and ceiling of the cooling chamber, and several short cylindrical nozzles are protruded from the bottom plenum chamber at a distance between the transport rolls and are inclined in the direction in which the heated object travels or in the opposite direction. From the plenum chamber in the ceiling, a short cylindrical nozzle that faces symmetrically with the above-mentioned nozzle is inclined in the same direction and protrudes, so that when the heated object is carried into the heating chamber and the cooling chamber, the subsequent heated object is The high-temperature non-oxidizing gas for heating and the low-temperature non-oxidizing gas for cooling are injected from both plenum chambers through the nozzles, respectively, with an appropriate interval between the objects to be heated. Long pipes or rod-shaped materials that generate dynamic pressure along the length of the heated object by colliding with each other to cause each non-oxidizing gas to flow into the inside of the pipe of the heated object or into the gap between the rod-shaped materials. Continuous atmosphere heat treatment method for heated objects.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP50111071A JPS5929643B2 (en) | 1975-09-13 | 1975-09-13 | Continuous atmosphere heat treatment furnace |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP50111071A JPS5929643B2 (en) | 1975-09-13 | 1975-09-13 | Continuous atmosphere heat treatment furnace |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5235110A JPS5235110A (en) | 1977-03-17 |
| JPS5929643B2 true JPS5929643B2 (en) | 1984-07-21 |
Family
ID=14551632
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP50111071A Expired JPS5929643B2 (en) | 1975-09-13 | 1975-09-13 | Continuous atmosphere heat treatment furnace |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5929643B2 (en) |
Families Citing this family (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB8303673D0 (en) * | 1983-02-10 | 1983-03-16 | Boc Group Plc | Heat treatment of workpieces |
| FR2583779A1 (en) * | 1985-06-25 | 1986-12-26 | Montaudon Patrick | Device for reducing the oxidation of objects placed in a gas treatment enclosure when they are extracted therefrom |
| JP2565570B2 (en) * | 1989-08-14 | 1996-12-18 | 株式会社 興研 | Ground fault current suppression method and device in three-phase water resistor |
| CA2615962C (en) | 2005-07-25 | 2011-04-26 | Sumitomo Metal Industries, Ltd. | Continuous heat treatment furnace and utilizing the same, metal pipe and method of heat treatment |
| JP5520571B2 (en) * | 2009-10-20 | 2014-06-11 | 新日鐵住金株式会社 | Hardened steel production equipment |
| JP5520570B2 (en) * | 2009-10-20 | 2014-06-11 | 新日鐵住金株式会社 | Equipment for manufacturing bending members made of hardened steel |
| CN105886719A (en) * | 2016-05-25 | 2016-08-24 | 内蒙古包钢钢联股份有限公司 | Method for controlling 16 Mn seamless steel tube blank heating |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5127210Y2 (en) * | 1972-02-29 | 1976-07-10 | ||
| US3738025A (en) * | 1972-07-31 | 1973-06-12 | Hanson Ind Inc | Ski boot having variable stiffness |
| JPS51122608A (en) * | 1975-04-19 | 1976-10-26 | Daido Steel Co Ltd | A gas replacement arrangement in continuous atmosphere heat treating f urnaces |
-
1975
- 1975-09-13 JP JP50111071A patent/JPS5929643B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5235110A (en) | 1977-03-17 |
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