JPS5919187B2 - Bright annealing method - Google Patents

Bright annealing method

Info

Publication number
JPS5919187B2
JPS5919187B2 JP53057314A JP5731478A JPS5919187B2 JP S5919187 B2 JPS5919187 B2 JP S5919187B2 JP 53057314 A JP53057314 A JP 53057314A JP 5731478 A JP5731478 A JP 5731478A JP S5919187 B2 JPS5919187 B2 JP S5919187B2
Authority
JP
Japan
Prior art keywords
furnace
gas
pressure
annealing
hydrogen
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
Application number
JP53057314A
Other languages
Japanese (ja)
Other versions
JPS54148112A (en
Inventor
繁三郎 中川
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.)
NAKAGAWA KK
Original Assignee
NAKAGAWA KK
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 NAKAGAWA KK filed Critical NAKAGAWA KK
Priority to JP53057314A priority Critical patent/JPS5919187B2/en
Publication of JPS54148112A publication Critical patent/JPS54148112A/en
Publication of JPS5919187B2 publication Critical patent/JPS5919187B2/en
Expired legal-status Critical Current

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Description

【発明の詳細な説明】 本発明は真ちゅうその他の銅合金を実質的に酸素を含有
しない水素ふん囲気中で光輝焼鈍する方法に関するもの
である。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for bright annealing brass and other copper alloys in a substantially oxygen-free hydrogen atmosphere.

従来真ちゅう線等の光輝焼鈍に当って(dベル炉又はポ
ット炉中で水素の還元ふん囲気中でこれを行っているが
、この場合大量の水素ガスを流して炉内の空気を置換し
なければなら々いので水素ガスの消費量が多くて不経済
であるのみならず、水素と空気中の酸素との混合による
爆発の危険もあり作業の安全管理の面で困難な問題をも
っている。
Conventionally, when bright annealing brass wire, etc., this is done in a hydrogen reducing atmosphere in a d-bell furnace or pot furnace, but in this case, a large amount of hydrogen gas must be flowed to replace the air in the furnace. Not only is this process uneconomical because it consumes a large amount of hydrogen gas, but there is also the risk of explosion due to the mixture of hydrogen and oxygen in the air, which poses a difficult problem in terms of work safety management.

又炉内ガスの露点をかなり下げておかないとガス中の水
分が焼鈍時に熱分解して金属材料の表面を酸化するので
十分な光輝焼鈍の効果は達成されない。
In addition, unless the dew point of the gas in the furnace is lowered considerably, moisture in the gas will thermally decompose during annealing and oxidize the surface of the metal material, so that a sufficient bright annealing effect will not be achieved.

そこで光輝焼鈍炉に比較的安価でしかも大量に還元性ふ
ん囲気を供給する方法として炉内でアンモニアクランキ
ングを行いちつ素と酸素との混合ガスふん囲気を現出す
る方法も提案されているが、この方法の場合そのふん囲
気ガス中から水分を除去してその露点を十分に下げるに
は複雑で高価な設備を必要とする。
Therefore, a method has been proposed in which ammonia cranking is performed in the furnace to generate a mixed gas atmosphere of nitrogen and oxygen as a relatively inexpensive and large quantity supplying reducing atmosphere to the bright annealing furnace. However, this method requires complex and expensive equipment to remove moisture from the ambient gas and sufficiently lower its dew point.

本発明はこのような問題点を解消するためになされたも
ので、以下これを詳述する。
The present invention has been made to solve these problems, and will be described in detail below.

光輝焼鈍すべき金属材料を収容した密閉焼鈍炉の内部を
−たん2mmH&程度の真空にしてから液体ちつ素から
のちつ素ガスと水素ボンベからの水素ガスを適宜に混合
して水素ガスの分圧4%前後の混合ガスとしたものを少
量宛注入し、これら混合ガスにより該金属材料並びに炉
内の脱酸素及び脱湿のための洗浄を減圧下に反覆して行
い、然る後焼鈍温度までの加熱昇温中は膨張する炉内の
ガス圧を逃すことも兼ねて焼鈍炉内に外圧よりも若干高
い内圧となるように上記のちり素と水素との混合ガスを
注入しその際一方の口からは内部のちつ素と水素ガスを
逃げるのを許すと共に該混合ガスを他方の口より補給し
て絶えず炉内の圧力を外圧よりも若干高めに維持せしめ
る。
The inside of the sealed annealing furnace containing the metal material to be brightly annealed is made to have a vacuum of about -2 mmH, and then nitrogen gas from liquid nitrogen and hydrogen gas from a hydrogen cylinder are appropriately mixed to separate hydrogen gas. A small amount of mixed gas at a pressure of around 4% is injected, and the mixed gas is used to repeatedly clean the metal material and the inside of the furnace for deoxidation and dehumidification under reduced pressure, and then the annealing temperature is lowered. During heating and temperature rise, the above-mentioned mixed gas of chiron and hydrogen was injected into the annealing furnace to release the expanding gas pressure inside the furnace so that the internal pressure was slightly higher than the external pressure. The nitrogen and hydrogen gas inside is allowed to escape from the opening, and the mixed gas is replenished from the other opening to constantly maintain the pressure inside the furnace slightly higher than the outside pressure.

そこで焼鈍温度、例えば真ちゅうの場合約500〜55
0℃に達したら暫時例えば30〜60分そのままの温度
に保持し、次に冷却の段階では炉内の収縮するガス体積
に見合う以上の混合ガスを供給して絶えず炉内圧力が外
圧より若干高くなるようにしておく。
Therefore, the annealing temperature, for example in the case of brass, is about 500 to 55
Once the temperature reaches 0°C, the temperature is maintained for a while, for example, 30 to 60 minutes, and then during the cooling stage, a mixed gas is supplied in an amount that is equal to or more than the shrinking gas volume in the furnace, so that the pressure inside the furnace is constantly raised slightly higher than the outside pressure. Let it be.

このようにしてちり素と水素の混合ふん囲気中で冷却し
てから金属材料を炉内より取出すことによって所期の光
輝焼鈍が達成される。
In this manner, the desired bright annealing is achieved by cooling the metal material in an atmosphere containing a mixture of chiron and hydrogen and then taking it out of the furnace.

本発明の実施において炉内をちつ素と水素との混合ガス
で洗浄するときの炉内の減圧度は0.01kplcr&
以下とするのが望丑しく、又この洗浄工程、焼鈍工程次
の冷却工程における水素ガスの分圧は4%程度で十分で
あり、前出の昇温工程、焼鈍工程1.冷却工程における
炉内外の圧力差は0.01kg/d程度であればよい。
In carrying out the present invention, the degree of pressure reduction in the furnace when cleaning the inside with a mixed gas of nitrogen and hydrogen is 0.01kplcr&
It is preferable that the partial pressure of hydrogen gas in the cleaning step and the cooling step following the annealing step is about 4%. The pressure difference between the inside and outside of the furnace in the cooling process may be about 0.01 kg/d.

以上本発明法による利点を要約して別記すると次の通り
である。
The advantages of the method of the present invention are summarized and separately described as follows.

(1) ちつ素源として液体ちつ素を用いているので
酸素含有量は非常に少く又水分も々いため焼鈍すべき金
属材料の酸化度が余り進んでいない場合には高価な水素
の使用量が非常に少くて済み経済的に極めて有利である
(1) Since liquid nitrogen is used as the nitrogen source, the oxygen content is very low and the moisture content is high, so if the degree of oxidation of the metal material to be annealed is not very advanced, expensive hydrogen may be used. It requires only a very small amount and is very economically advantageous.

(2)シかも焼鈍工程及びその前後の工程を水素ガスの
分圧4%程度の水素とちつ素との混合ガス中で実施する
ので爆発限界外で操業できるので作業管理面で極めて有
利であり、又低コストで実施できることにもなる。
(2) Since the annealing process and the processes before and after it are carried out in a mixed gas of hydrogen and nitrogen with a partial pressure of hydrogen gas of about 4%, it is possible to operate outside the explosion limit, which is extremely advantageous in terms of work management. It also means that it can be implemented at low cost.

(3)焼鈍炉内を−たん2朋刃位にまで真空にしてから
上記の混合ガスで0.01 kg/cyrt程度の減圧
下で反覆して炉内を洗浄するので金属材料に付着ないし
発生していた或いは炉内に残存していた微量の酸素ガス
及び水分を系外に除去できるので、次の焼鈍工程では水
素ガスの分圧が低い混合ガスふん囲・気中でも十分な光
輝焼鈍の効果が達成される。
(3) The inside of the annealing furnace is evacuated to a level of -2 mm, and then the above mixed gas is repeatedly used under a reduced pressure of about 0.01 kg/cyrt to clean the inside of the furnace. Trace amounts of oxygen gas and moisture remaining in the furnace can be removed from the system, so in the next annealing process, the effect of bright annealing is sufficient even in a mixed gas atmosphere or air where the partial pressure of hydrogen gas is low. is achieved.

((1)昇温工程、焼鈍工程及び冷却工程では炉内の混
合ガスの圧力を絶えず外圧よりも0.01kg/d程度
高くしているので炉内に外気の入り込むおそれもなく安
全であり、又所望の光輝焼鈍の効果が保証される。
((1) In the temperature raising process, annealing process, and cooling process, the pressure of the mixed gas in the furnace is constantly raised to about 0.01 kg/d higher than the external pressure, so there is no risk of outside air entering the furnace and it is safe. Moreover, the desired bright annealing effect is guaranteed.

(5)少量の混合ガスで炉内及び炉内の金属材料を予め
洗浄する予備工程を設けたことにより光輝焼鈍の工程(
その前後の昇温及び冷却も含む)に使用される混合ガス
の使用量が極めて少くて済み、しかも高価な水素ガスは
該混合ガス中4%前後と少量であるので、一層有利であ
り、かつ安全である等その工業的価値大である。
(5) Bright annealing process (
The amount of mixed gas used for heating and cooling (including heating and cooling before and after) is extremely small, and the amount of expensive hydrogen gas is only around 4% of the mixed gas, which is even more advantageous. It is safe and has great industrial value.

以下に本発明の実施例を示す。Examples of the present invention are shown below.

F−1の第1図において9は伸線機で伸線した丹銅(C
u85%)の線材を示しこれを約500に90線束(コ
イルでもよい)、としである。
In Fig. 1 of F-1, 9 is red copper (C) drawn with a wire drawing machine.
This is a wire rod of about 500 to 90 wires (a coil may be used).

この線材9は伸線の際には予め約300℃で完全に蒸発
し、じみの原因となる残渣を残さぬような潤滑剤を用い
ること、及び、捲ル装置前に拭取装置を設置して余分の
油等を出来るだけ拭取っておくことが肝要である。
When drawing the wire 9, it is necessary to use a lubricant that completely evaporates at approximately 300°C and leaves no residue that may cause bleeding, and to install a wiping device in front of the winding device. It is important to wipe off as much excess oil as possible.

トリクレーンによる脱脂は概して行わ々い方がよく、適
宜な油を選び且つよく拭取れば、線材表面に微量に油分
が残っていても、又それを密にコイル等に捲取っても真
空下に加熱することにより蒸発して仕上りに余り影響な
い。
It is generally better not to degrease with a tri-crane.If you choose an appropriate oil and wipe it off thoroughly, even if there is a small amount of oil left on the surface of the wire, or if it is tightly wound around a coil etc., it will not work under vacuum. When heated, it evaporates and does not affect the finish much.

このような線材9を架台2の上に設けられた下部電気炉
8上に架設されたポール10に引かけて積むがポール1
0は束が崩れないように積むだめのものであり、その他
製品によっては適宜に設けられた棚等が用いられる。
Such wire rods 9 are stacked by hooking them onto a pole 10 installed on a lower electric furnace 8 installed on a pedestal 2.
0 is for stacking the bundles to prevent them from collapsing, and depending on the product, an appropriately provided shelf or the like may be used.

次にマツプル(保護容器)3をクレーンで吊上げて、電
気炉1にかぶせてから、締、金6を締めて、マツフルと
炉台間を密封する。
Next, the Matsupuru (protective container) 3 is lifted up by a crane and placed over the electric furnace 1, and then the clamp 6 is tightened to seal the space between the Matsufuru and the furnace stand.

マツフルの内径は約1l100ix、高さ1400mm
内容積約1,3001である。
The inner diameter of Matsuful is approximately 1l100ix, and the height is 1400mm.
The internal volume is approximately 1,3001.

浄却管7に水を流し、次いでベル型電気炉1のスイッチ
を入れ、加熱を開始すると同時に第2図に示す真空ポン
プ13のスイッチを入れる。
Water is flowed through the purification pipe 7, then the bell-shaped electric furnace 1 is turned on, and at the same time as heating is started, the vacuum pump 13 shown in FIG. 2 is turned on.

伺その前にバルブV−3をしめV−1を開けるが、バル
ブV−2、V−4、V−5は閉まっている。
Before that, I close valve V-3 and open V-1, but valves V-2, V-4, and V-5 are closed.

約10分層にはマツフル3内の温度は50°C以上に達
する、又真空度は2−3siH5となる。
After about 10 minutes, the temperature inside Matsufuru 3 reaches 50°C or more, and the degree of vacuum becomes 2-3siH5.

そこでバルブV−4、V−5を開け、微量注入バイパス
回路14の圧力を調整して、極めて少量ずつ例えば約1
31/分の速度で混合ガスを流して、マツフル内の残量
空気を完全に置換する(約10分間)。
Then, open the valves V-4 and V-5, adjust the pressure of the microinjection bypass circuit 14, and inject a very small amount, for example, about 1.
Flow the mixed gas at a rate of 31/min to completely replace the remaining air in the Matsufuru (about 10 minutes).

この際真空度を8iiwI即ち、0.01ゆ72以上に
ならぬように注意する。
At this time, care must be taken to ensure that the degree of vacuum does not exceed 8iiwI, that is, 0.01y72.

混合ガスは液体ちつ素タンク15からのN2 と水素ボ
ンベ16からのN2を容量比96:4位にしたもので、
自動混合装置17で混合を行い、レシーバタンク18に
貯められる。
The mixed gas is N2 from the liquid nitrogen tank 15 and N2 from the hydrogen cylinder 16 in a volume ratio of about 96:4.
The mixture is mixed in an automatic mixing device 17 and stored in a receiver tank 18 .

この操作で、一気圧下だと10回マツフル内の空気を交
換するに要する13m3のガスの17100の0.13
m’でもって同様の比率で02の含有率を下げることが
出来又気圧がo、 01 kg/cr7を以下なので更
に1/100以下に0□■ 含有率を下げることが出来る。
With this operation, 0.13 of 17100 of the 13 m3 of gas required to exchange the air in the Matsufuru 10 times under one atmospheric pressure.
The content of 02 can be lowered by the same ratio with m', and since the atmospheric pressure is less than 01 kg/cr7, it is possible to further reduce the content of 0□■ to 1/100 or less.

即ち□のガス00 で100倍の効果を上げることが出来、もし、N2+H
2ガス中の02含有量がippm以下なら略マツフル内
の02含有量もIPPm以下にすることが出来る。
In other words, □ gas 00 can increase the effect 100 times, and if N2+H
If the 02 content in the two gases is ippm or less, the 02 content in the almost Matsufuru can also be made to be IPPm or less.

、次にバルブV−1をしめ真空ポンプのスイッチを切り
、バルブV−4をしめバルブV−2を開け、急速にマツ
フル内にガスを充たす。
Next, close the valve V-1 to turn off the vacuum pump, close the valve V-4, and open the valve V-2 to rapidly fill the Matsufuru with gas.

真空ゲージ24は760 mrnflj9に戻り、マツ
フル内の温度の上昇につれて7〜10rILnHfl/
分ノ速度で内圧が上昇してくる。
The vacuum gauge 24 returns to 760 mrnflj9, and as the temperature inside Matsuful rises, it increases to 7 to 10 rILnHfl/
The internal pressure rises at a rate of 1 minute.

バルブV−2を締め、真空ゲージ24によって上昇する
内圧(正圧)が約8mmwI (0,01kg/d)以
内に止まるように、バルブV−3を開き、膨張するガス
を逃がす。
Close the valve V-2, and open the valve V-3 to release the expanding gas so that the internal pressure (positive pressure) rising by the vacuum gauge 24 is stopped within about 8 mmwI (0.01 kg/d).

(0〜181/分)、約2時間でマツフル内の温度は丹
銅線の十分な焼鈍温度である550℃に達する。
(0 to 181/min), and the temperature inside the Matsufuru reaches 550° C., which is a sufficient annealing temperature for red copper wire, in about 2 hours.

バルブV−4を再び開き、微量バイパス14を用いて微
量のガスを補給しながら、約1時間そのままに保つ。
Valve V-4 is reopened and held there for approximately 1 hour, using trace bypass 14 to replenish trace amounts of gas.

約1時間の保持時聞届に電気炉のスイッチを切り、クレ
ーンで吊り上げて除く、マツフルを急速に冷却するには
冷却フードをかぶせて冷水噴霧を行うか、冷風を吹付け
る。
After holding for about an hour, turn off the electric furnace and lift it with a crane to remove it.To quickly cool down the Matsufuru, cover it with a cooling hood and spray with cold water or blow cold air.

この際常に微量ガス注入バイパス14の圧力を調整して
、マツフル内が減圧状態にならないように注意する。
At this time, always adjust the pressure of the trace gas injection bypass 14 to ensure that the inside of the matsuful does not become depressurized.

マツフル内の温度が50℃位まで下がってから微量バイ
パス14を閏じ、バルブV−3を開いて空気を注入し、
マツフルを除き、品物を取出す。
After the temperature inside Matsuful has dropped to about 50℃, the slight bypass 14 is opened, the valve V-3 is opened, and air is injected.
Remove the items, excluding the matsufuru.

丹銅線は完全に焼鈍され、(抗張力約28〜30kg/
ma)且つその光沢、色沢は全く損われない。
The red copper wire is completely annealed and has a tensile strength of approximately 28~30kg/
ma) and its gloss and color are not impaired at all.

真ちのう線(65%Cu735%Znの場合)は550
℃ではZnの蒸発が激しいためか光沢が失われるので、
500℃以下で行った方がよい。
The true line (in the case of 65%Cu735%Zn) is 550
At ℃, the luster is lost, probably due to rapid evaporation of Zn.
It is better to do this at a temperature below 500°C.

470℃位で行うと、美麗な光沢が損われない。If done at around 470°C, the beautiful luster will not be lost.

以上の如く、本発明の方法によると、 ■−使用するガス量が極めて少ないにも拘らず(上記5
00kyの焼鈍において、96%N2+4%N2ガスの
使用量は一回最大4m’にすぎない)■ 液体ちつ素か
らのN2ガスを主成分とし、N2ガスを約4%含む、極
めて安全なガス(N2の爆発限界4.1%)であると同
時に、マツフル内の空気即ち0□を置換除去することが
出来る。
As described above, according to the method of the present invention, (1) Despite the extremely small amount of gas used (see above 5.
In 00ky annealing, the amount of 96%N2 + 4%N2 gas used is only 4m' at maximum at one time) ■ Extremely safe gas whose main component is N2 gas from liquid nitrogen and contains approximately 4% N2 gas. (The explosion limit of N2 is 4.1%), and at the same time, it is possible to displace and remove the air in the Matsufuru, that is, 0□.

■ 同時に揮発性の油を除いて、色沢に悪影響を与えな
い。
■ At the same time, excluding volatile oils, there is no negative effect on color luster.

■ 極めて光沢のある、又色沢においても優れたCu合
金の焼鈍が行われる。
■ Cu alloys can be annealed with extremely high gloss and excellent color.

■ 設備費、ガス代共コストが安く酸洗及びそれに伴う
手間と、公害防止費用を勘案すると非常に経済的である
■Equipment costs and gas costs are both low, making it extremely economical considering the pickling process, the associated labor, and pollution prevention costs.

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

第1図は本発明方法の実施に用いられた光輝焼鈍炉の断
面見取図、第2図は本発明方法の実施例における回路図
である。 1・・・・・・ベル型電気炉、2・・・・・・架台、3
・・・・・・マツフル、4・・・・・・ゴムバッキング
、5・・・・・・耐熱シール、6・・・・・・締金、7
・・・・・・冷却管、8・・・・・・下部電気炉、9・
・・・・・線材、10・・・・・・ポール、11・・・
・・・ガス入口、12・・・・・・排気口、13・・・
・・・真空ポンプ、14・・・・・・微量注入バイパス
、15・・・・・・液体ちつ素タンク、16・・・・・
・水素ボンベ−17・・・・・・自動ガス定量混合装置
、18・・・・・・レシーバタンク、19・・・・・・
流量計(容量0〜301/分)、19′・・・・・・流
量計、20・・・・・・一次圧力調整器、21・・・・
・・二次圧力調整器、22・・・・・・圧力調整器およ
びバルブ、23・・・・・・逆止弁、24・・・・・・
バツキュームゲージ、25・・・・・・マノメータ、2
6・・・・・・レリーズバ/lz7”、V−1〜V−5
・・・・・・バルブ。
FIG. 1 is a cross-sectional diagram of a bright annealing furnace used in carrying out the method of the present invention, and FIG. 2 is a circuit diagram of an embodiment of the method of the present invention. 1... Bell-shaped electric furnace, 2... Frame, 3
...Matsuful, 4...Rubber backing, 5...Heat-resistant seal, 6...Clamp, 7
......Cooling pipe, 8...Lower electric furnace, 9.
...Wire, 10...Pole, 11...
...Gas inlet, 12...Exhaust port, 13...
...Vacuum pump, 14...Micro injection bypass, 15...Liquid nitrogen tank, 16...
・Hydrogen cylinder - 17... Automatic gas quantitative mixing device, 18... Receiver tank, 19...
Flowmeter (capacity 0 to 301/min), 19'...Flowmeter, 20...Primary pressure regulator, 21...
...Secondary pressure regulator, 22...Pressure regulator and valve, 23...Check valve, 24...
Vacuum gauge, 25... Manometer, 2
6... Release bar/lz7", V-1 to V-5
······valve.

Claims (1)

【特許請求の範囲】[Claims] 1 真鍮等の銅合金を実質的に酸素を含有しない水素雰
囲気中で光輝焼鈍するに際し、上記の金属材料を収容し
た密閉焼鈍炉内を一旦真空にしてから液体窒素からの窒
素ガスと水素ポンプからの水素ガスを混合して水素ガス
の分圧を4%程度とした混合ガスを炉内に少量宛供給し
てこれら混合ガスにより該金属材料並びに炉内の脱酸素
及び脱湿のための洗浄を0.01kg/ffl程度の減
圧下に反覆して行ない、然る後この焼鈍炉内に外圧より
も高い内圧となるように上記の混合ガスを供給し、かつ
この混合ガスを補給しながら外圧よりも0.01kg/
cr?L程度の高い内圧を維持して炉内を金属材料の焼
鈍温度まで昇温保持し引続き同一圧力条件下に冷却して
から金属材料を炉内より取出すことを特徴とする光輝焼
鈍法。
1 When bright annealing copper alloys such as brass in a hydrogen atmosphere that does not substantially contain oxygen, the inside of the closed annealing furnace containing the above metal materials is first evacuated, and then nitrogen gas from liquid nitrogen and a hydrogen pump are used. A small amount of mixed gas with a hydrogen gas partial pressure of about 4% is supplied into the furnace, and these mixed gases are used to clean the metal materials and the inside of the furnace for deoxidation and dehumidification. The annealing process is repeated under a reduced pressure of about 0.01 kg/ffl, and then the above-mentioned mixed gas is supplied into the annealing furnace so that the internal pressure is higher than the external pressure, and while replenishing this mixed gas, the external pressure is lowered. Also 0.01kg/
cr? A bright annealing method characterized by maintaining a high internal pressure of about L, increasing the temperature in the furnace to the annealing temperature of the metal material, and then taking out the metal material from the furnace after cooling under the same pressure condition.
JP53057314A 1978-05-15 1978-05-15 Bright annealing method Expired JPS5919187B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP53057314A JPS5919187B2 (en) 1978-05-15 1978-05-15 Bright annealing method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP53057314A JPS5919187B2 (en) 1978-05-15 1978-05-15 Bright annealing method

Publications (2)

Publication Number Publication Date
JPS54148112A JPS54148112A (en) 1979-11-20
JPS5919187B2 true JPS5919187B2 (en) 1984-05-02

Family

ID=13052097

Family Applications (1)

Application Number Title Priority Date Filing Date
JP53057314A Expired JPS5919187B2 (en) 1978-05-15 1978-05-15 Bright annealing method

Country Status (1)

Country Link
JP (1) JPS5919187B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6144089U (en) * 1984-08-27 1986-03-24 一夫 藤村 Flexible joint for hume pipe

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6033188B2 (en) * 1980-09-30 1985-08-01 石川島播磨重工業株式会社 Metal heat treatment equipment
US4511410A (en) * 1984-04-02 1985-04-16 Olin Corporation Copper-tin alloys having improved wear properties
US4586967A (en) * 1984-04-02 1986-05-06 Olin Corporation Copper-tin alloys having improved wear properties
US6464809B2 (en) * 1998-11-30 2002-10-15 Outokumpu Oyj Processes for producing articles with stress-free slit edges
CN102260837B (en) * 2011-07-07 2013-03-06 安徽精诚铜业股份有限公司 Protective atmosphere switching method for red copper and brass strips

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4838214A (en) * 1971-09-17 1973-06-05

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4838214A (en) * 1971-09-17 1973-06-05

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6144089U (en) * 1984-08-27 1986-03-24 一夫 藤村 Flexible joint for hume pipe

Also Published As

Publication number Publication date
JPS54148112A (en) 1979-11-20

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