JPH0681097A - Method for galvanizing oxidized scale adhered steel worked product - Google Patents

Method for galvanizing oxidized scale adhered steel worked product

Info

Publication number
JPH0681097A
JPH0681097A JP25566092A JP25566092A JPH0681097A JP H0681097 A JPH0681097 A JP H0681097A JP 25566092 A JP25566092 A JP 25566092A JP 25566092 A JP25566092 A JP 25566092A JP H0681097 A JPH0681097 A JP H0681097A
Authority
JP
Japan
Prior art keywords
hot
galvanizing
atmosphere
dip galvanizing
pretreatment
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
Application number
JP25566092A
Other languages
Japanese (ja)
Other versions
JP2611175B2 (en
Inventor
Ichiro Nakamura
一郎 中村
Akihiko Maekita
杲彦 前北
Shuichi Ito
修一 伊藤
Nobuhiro Abe
信浩 阿部
Haruzo Shudo
治三 首藤
Takashi Nagao
隆 長尾
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.)
ESUTEMU KK
Shinsei Industries Co Ltd
OM Industry Co Ltd
Shinsei Kogyo KK
Original Assignee
ESUTEMU KK
Shinsei Industries Co Ltd
OM Industry Co Ltd
Shinsei Kogyo 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 ESUTEMU KK, Shinsei Industries Co Ltd, OM Industry Co Ltd, Shinsei Kogyo KK filed Critical ESUTEMU KK
Priority to JP25566092A priority Critical patent/JP2611175B2/en
Publication of JPH0681097A publication Critical patent/JPH0681097A/en
Application granted granted Critical
Publication of JP2611175B2 publication Critical patent/JP2611175B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Abstract

PURPOSE:To improve the operating environment by heating a worked product in an oxidizing atmosphere to burn adhered material and thereafter subjecting it to pretreatment in which reduction and temp. control are executed under specified conditions. CONSTITUTION:In the method for galvanizing in which a hot rolled oxide scale adhered steel worked product is subjected to pretreatment, is thereafter immersed in a galvanizing bath of 430 to 530 deg.C, is plated, is subsequently discharged from the plating bath and is freed from surplus adhered zinc, pretreatment is executed in such a manner that the worked product is heated in an oxidizing atmosphere to burn the adhered material, and after that, it is reduced at 400 to 800 deg.C in an atmosphere of a reducing gas and is thereafter subjected to temp. control to <=560 deg.C in an atmosphere of a nonoxidizing gas. In this way, the environment of the galvanizing operation for the oxidized scale adhered steel worked product can be improved.

Description

【発明の詳細な説明】Detailed Description of the Invention

【001】[001]

【産業上の利用分野】本発明は、前処理に酸化スケ−ル
をデスケ−ルせずに還元性ガスにより直接還元する方法
を用いた熱延酸化スケ−ル付着鉄鋼加工品の溶融亜鉛め
っき方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to hot dip galvanizing of hot-rolled oxide scale-adhered steel products using a method in which pre-treatment is carried out by directly reducing the oxide scale with a reducing gas without descaling. Regarding the method.

【002】[002]

【従来技術】熱延したままの黒皮熱延鋼板に成形加工や
溶接加工を施して製造した鉄鋼加工品は、多くの場合、
錆止め塗装を施して使用されるが、橋梁、地下鉄駅、ト
ンネルなどのような外観と耐食性を必要とする用途に使
用される場合は、従来より溶融亜鉛めっきを施してい
る。
2. Description of the Related Art In many cases, steel products manufactured by subjecting hot-rolled black skin hot-rolled steel sheet to forming and welding
It is used after being coated with rust-preventive paint, but when it is used for applications requiring appearance and corrosion resistance such as bridges, subway stations, tunnels, etc., it has been hot-dip galvanized.

【003】ところで、鉄鋼加工品(以下単に加工品とい
う)は、製造の際に成形加工機を使用したりするので、
機械油が付着していたり、部材番号が塗料で記入されい
たりする場合がある。また、製造には屋外に放置してお
いた熱延鋼板を使用したり、加工品も屋外に放置したり
するので、熱延スケ−ルの黒錆が一部赤錆に変化し、酸
化スケ−ルは黒錆、赤錆の混在したものになっている。
このため、溶融亜鉛めっきするにあたっては前処理で機
械油や黒錆、赤錆を除去していた。
By the way, since a processed steel product (hereinafter simply referred to as a processed product) uses a molding machine in manufacturing,
Machine oil may be attached or the part number may be marked with paint. In addition, because hot rolled steel sheets left outdoors during manufacturing are used and processed products are also left outdoors, black rust in the hot rolled scale partially changes to red rust, which causes oxidation scale. Le is a mixture of black rust and red rust.
For this reason, machine oil, black rust, and red rust were removed by pretreatment before hot-dip galvanizing.

【004】この前処理は、有機溶剤やアルカリによる脱
脂処理で機械油をまず除去して、水洗した後、塩酸や塩
酸と硫酸の混酸による酸洗処理で10分間以上デスケ−
ルして、水洗後フラックス処理する方法で行っていた
が、この前処理では、脱脂処理装置からは有機溶剤やア
ルカリのヒュ−ムが常時発生し、また、酸洗処理装置か
らは処理の都度酸や反応ガスが多量に発生する。
In this pretreatment, the mechanical oil is first removed by degreasing treatment with an organic solvent or alkali, followed by washing with water, and then pickling treatment with hydrochloric acid or a mixed acid of hydrochloric acid and sulfuric acid for 10 minutes or more.
However, in this pretreatment, fumes of organic solvent and alkali are constantly generated from the degreasing treatment equipment, and from the pickling treatment equipment each time treatment is performed. A large amount of acid and reaction gas are generated.

【005】[0095]

【発明が解決しようとする問題点】しかしながら、加工
品は、形状や寸法が一定していないため、各処理を密閉
装置で実施できず、解放装置で実施しなければならな
い。また、加工品の移動も形状や寸法の関係で自動化で
きず、作業者によらなければならない。このため、前処
理区域での作業環境や作業条件は非常に悪いものであつ
たが、脱脂処理装置からのヒュ−ムや酸洗処理装置から
の酸、反応ガスを防止もしくは抑制する有効な手段がな
いのが実状であった。また、前処理を施すと、廃液が多
量に発生するが、廃液は無害化処理を施さねばならない
ため、その処理に多額の費用がかかるという問題もあっ
た。
However, since the processed product has a non-uniform shape and size, each process cannot be carried out by the sealing device and must be carried out by the releasing device. Further, the movement of the processed product cannot be automated due to the shape and the size, and it must be done by the operator. For this reason, the working environment and working conditions in the pretreatment area were extremely poor, but an effective means for preventing or suppressing fumes from the degreasing treatment equipment and acids and reaction gases from the pickling treatment equipment. The reality was that there was no. Further, when pretreatment is performed, a large amount of waste liquid is generated, but since the waste liquid must be subjected to detoxification treatment, there is a problem that the treatment requires a large amount of money.

【006】さらに、溶融亜鉛めっきの際には、加工品に
より異なるが、浴温430〜530℃のめっき浴中に3
〜30分間も加工品を浸漬しなければならないので、浸
漬中フラックス分解による刺激臭の白煙が発生する。し
かし、めっき浴も解放型にしなければならないため、白
煙がめっき浴区域の作業環境を悪化させていた。
Further, in the hot dip galvanizing, depending on the processed product, 3 in a plating bath having a bath temperature of 430 to 530 ° C.
Since the processed product must be soaked for about 30 minutes, white smoke with an irritating odor is generated due to flux decomposition during the soaking. However, since the plating bath also has to be an open type, white smoke deteriorates the working environment in the plating bath area.

【007】[0097]

【問題点を解決するための手段】本発明は、これらの問
題を解消した加工品の溶融亜鉛めっき方法を提供するも
のである。すなわち、本発明は、前処理を、加工品を酸
化性雰囲気中で加熱して、付着物を燃焼させた後、還元
性ガス雰囲気中にて400〜800℃で還元し、その
後、非酸化性ガス雰囲気中で560℃以下になるように
温度調整する方法で行うことにした。
SUMMARY OF THE INVENTION The present invention provides a hot dip galvanizing method for processed products which solves these problems. That is, in the present invention, in the pretreatment, the processed product is heated in an oxidizing atmosphere to burn the deposits, and then reduced at 400 to 800 ° C. in a reducing gas atmosphere, and then the non-oxidizing property is applied. It was decided to perform the method by adjusting the temperature so that the temperature would be 560 ° C. or lower in a gas atmosphere.

【008】[0085]

【作用】ガス還元方式の連続溶融亜鉛めっきラインで
は、冷延鋼板を前処理帯で加熱して、不純物を酸化除去
し、その後水素ガスと窒素ガスとの混合ガスで還元する
前処理法が行われているが、この場合、加熱により発生
する酸化スケ−ルは薄く、通常0.1μm以下で、熱延
酸化スケ−ルのように厚くない。このため、水素ガスを
含有する還元性ガスで還元できるが、熱延酸化スケ−ル
の黒錆(Fe34)は5〜10μmと厚く、緻密で、そ
の酸化による赤錆[Fe23やFe(OH)3など]はさ
らに厚いので、従来その除去は酸洗によらなければ、困
難であるとされていた。
[Operation] In the gas reduction type continuous hot dip galvanizing line, a pretreatment method is performed in which the cold-rolled steel sheet is heated in the pretreatment zone to oxidize and remove impurities, and then reduced with a mixed gas of hydrogen gas and nitrogen gas. However, in this case, the oxide scale generated by heating is thin, usually 0.1 μm or less, and not as thick as the hot rolled oxide scale. Therefore, although it reduced with a reducing gas containing hydrogen gas, hot rolling oxide scale - black Le rust (Fe 3 O 4) is as thick as 5 to 10 [mu] m, a dense, red rust [Fe 2 O 3 by oxidation And Fe (OH) 3 etc.] are thicker, it has been conventionally considered difficult to remove them without pickling.

【009】しかしながら、本発明者らは、これらの熱延
酸化スケ−ルの水素ガスまたはその含有混合ガスによる
還元を検討したところ、還元予備処理を工夫すれば、黒
錆、赤錆とも比較的短時間に還元できることを見いだし
た。
However, the present inventors examined the reduction of these hot-rolled oxide scales with hydrogen gas or a mixed gas containing them, and as a result of devising the reduction pretreatment, both black rust and red rust were relatively short. I found that I could return it in time.

【010】図1および図2は、黒錆酸化スケ−ル厚みが
5〜10μmの低炭素熱延鋼板(板厚2.2mm)を水
素ガスと窒素ガスの混合ガス中にてそれぞれ500℃お
よび600℃で直接還元した場合の水素ガス濃度と還元
時間による溶融亜鉛めっき性を示したものであるが、○
が両面良好めっき、△が片面不めっき、×が両面不めっ
きを示している。
FIGS. 1 and 2 show a low carbon hot rolled steel sheet having a black rust oxide scale thickness of 5 to 10 μm (sheet thickness 2.2 mm) in a mixed gas of hydrogen gas and nitrogen gas at 500 ° C. and It shows the hot dip galvanizability depending on the hydrogen gas concentration and the reduction time when directly reduced at 600 ° C.
Indicates good plating on both sides, △ indicates unplated on one side, and × indicates unplated on both sides.

【011】これらの結果によれば、酸化スケ−ルが黒錆
の場合、還元温度を500〜600℃にして、水素ガス
濃度2%以上の混合ガスで30〜240秒直接還元して
も、良好な溶融亜鉛めっきを施すことができる。この還
元時間は、従来の酸洗時間の10分以上に比べると、著
しく短い。
According to these results, when the oxide scale is black rust, the reduction temperature is set to 500 to 600 ° C., and the mixture is directly reduced for 30 to 240 seconds with a mixed gas having a hydrogen gas concentration of 2% or more. Good hot-dip galvanizing can be performed. This reduction time is significantly shorter than the conventional pickling time of 10 minutes or longer.

【012】しかしながら、加工品表面に機械油や塗料の
ような有機物が付着した状態で直接還元しても、雰囲気
が還元性であるため、有機物は炭化されるだけで、炭素
や顔料が残り、還元されないことが判明した。また、黒
錆は比較的短時間に還元されるが、赤錆は黒錆に比べる
と、還元性が劣り、黒錆と同一条件で還元しても、未還
元部分が残り、めっき不良部分が発生することも判明し
た。
However, even if the surface of the processed product is directly reduced with an organic substance such as machine oil or paint attached, the atmosphere is reductive and the organic substance is only carbonized, leaving carbon and pigments. It turned out not to be reduced. Also, black rust is reduced in a relatively short time, but red rust is less reducible than black rust, and even if it is reduced under the same conditions as black rust, unreduced parts remain and defective plating parts occur. It turned out to do.

【013】そこで、本発明者等は、かかる対策として、
還元処理前に酸化性雰囲気中で有機物を燃焼除去できる
温度に加熱したところ、赤錆の還元性も改善できること
を見いだしたのである。すなわち、酸化性雰囲気中で加
工品を高温に加熱すれば、機械油や樹脂は燃焼して、煙
りになって除去される。また、顔料が無機顔料でもマト
リックスの炭素がなくなるので、脱落してしまう。一
方、赤錆の還元性が改善されるのは、還元されにくいF
e(OH)3が脱水されて、還元され易いFe23に変化
するとともに、パウダリング化して表層が落下して、厚
みが薄くなり、次の還元工程で内部まで還元されてしま
うためと考えられる。
Therefore, the present inventors, as a countermeasure,
It was found that the reduction property of red rust can be improved by heating to a temperature at which organic substances can be burned and removed in an oxidizing atmosphere before the reduction treatment. That is, when the processed product is heated to a high temperature in an oxidizing atmosphere, the machine oil and resin are burnt and become smoke to be removed. Further, even if the pigment is an inorganic pigment, the carbon in the matrix is lost, so that it falls off. On the other hand, the reduction property of red rust is improved because it is difficult to reduce F
This is because e (OH) 3 is dehydrated and changed to Fe 2 O 3 which is easily reduced, and at the same time, the surface layer drops due to powdering, the thickness becomes thin, and it is reduced to the inside in the next reduction step. Conceivable.

【014】上記還元予備処理は、窒素ガス雰囲気のよう
な不活性ガス雰囲気中で実施しても効果がなく、酸化性
雰囲気中で実施することを必要とする。酸化性雰囲気と
しては大気でよい。加熱温度は、付着物の種類により決
定するが、機械油や塗料が一般的なものであれば、10
0℃以上、好ましくは200〜800℃にすればよい。
The above reduction pretreatment has no effect even if it is carried out in an inert gas atmosphere such as a nitrogen gas atmosphere, and it is necessary to carry out it in an oxidizing atmosphere. Air may be used as the oxidizing atmosphere. The heating temperature is determined by the type of deposit, but if the machine oil or paint is common, the heating temperature is 10
The temperature may be 0 ° C or higher, preferably 200 to 800 ° C.

【015】また、図3は、黒皮熱延鋼板に機械油と塗料
を塗布して、塩酸ヒュ−ムにさらし、黒錆を赤錆に変化
させた後、300℃の大気中で3分間加熱して、前記黒
皮熱延鋼板の場合と同様の混合ガスで還元した場合の溶
融亜鉛めっき性を示したものであるが、溶融亜鉛めっき
性は酸化スケ−ルが黒錆の場合と同様になっていること
がわかる。
FIG. 3 shows that black skin hot rolled steel sheet was coated with mechanical oil and paint, exposed to fume hydrochloride to change black rust into red rust, and then heated in air at 300 ° C. for 3 minutes. Then, it shows the hot-dip galvanizing property when reduced with the same mixed gas as in the case of the black skin hot-rolled steel sheet, the hot-dip galvanizing property is the same as when the oxide scale is black rust. You can see that it has become.

【016】なお、図1、図2の溶融亜鉛めっき性は、図
4に示すような実験装置により調査した。すなわち、上
下方向に伸長した密閉型石英製の円筒1の内部に上下動
可能な試験片保持棒2を上部から挿入して、その試験片
保持棒2の下側に試験片3を取り付けた後、円筒1の内
部に混合ガスを充たして、円筒1の外周に配置した赤外
線炉4で円筒1を加熱した。そして、試験片3が所定温
度になったら、赤外線炉4での加熱を中止して、480
℃になるまで冷却し、円筒1の下部を開き、円筒1の下
側に配置した浴温450℃の亜鉛めっき浴5に試験片保
持棒2とともに試験片3を落下させ、30秒間浸漬し
た。
The hot-dip galvanizing properties of FIGS. 1 and 2 were investigated by an experimental apparatus as shown in FIG. That is, after inserting the vertically movable test piece holding rod 2 into the inside of the closed quartz cylinder 1 extending vertically and attaching the test piece 3 to the lower side of the test piece holding rod 2. The cylinder 1 was filled with the mixed gas, and the cylinder 1 was heated by the infrared furnace 4 arranged on the outer periphery of the cylinder 1. Then, when the test piece 3 reaches a predetermined temperature, heating in the infrared furnace 4 is stopped and 480
The cylinder 1 was cooled to 0 ° C., the lower part of the cylinder 1 was opened, and the test piece 3 was dropped together with the test piece holding rod 2 into the zinc plating bath 5 having a bath temperature of 450 ° C. arranged under the cylinder 1 and immersed for 30 seconds.

【017】一方、図3の溶融亜鉛めっき性は、図4に示
す実験装置において、円筒1の内部を大気雰囲気にし
て、試験片3を加熱した後、窒素ガスで大気を一旦置換
し、その後混合ガスを導入して還元、溶融めっきする方
法で行った。
On the other hand, in the hot dip galvanizing property of FIG. 3, in the experimental apparatus shown in FIG. 4, the inside of the cylinder 1 was placed in the atmosphere, the test piece 3 was heated, and then the atmosphere was once replaced with nitrogen gas. The method was carried out by introducing a mixed gas, reducing and hot dipping.

【018】混合ガスによる還元は、加工品を400〜8
00℃、好ましくは450〜650℃に加熱して行う。
400℃未満であると、水素ガス濃度を高くしてもスケ
−ルの還元が困難になり、800℃を超えると、加工品
が変形したり、機械的性質が損なわれたりする可能性が
ある。また、水素ガス濃度は、図2に示すように、2%
以上であれば、還元できるので、100%でもよい。還
元後は加工品温度が高いと、溶融めっき中に合金層が著
しく発達して、めっき付着量が過度に厚くなってしまう
ので、560℃以下に冷却する。
The reduction with the mixed gas is carried out by using the processed product at 400 to 8
It is performed by heating to 00 ° C, preferably 450 to 650 ° C.
If it is less than 400 ° C, it becomes difficult to reduce the scale even if the hydrogen gas concentration is increased, and if it exceeds 800 ° C, the processed product may be deformed or the mechanical properties may be impaired. . The hydrogen gas concentration is 2% as shown in FIG.
If it is above, since it can be reduced, it may be 100%. After the reduction, if the temperature of the processed product is high, the alloy layer is remarkably developed during the hot dip plating, and the coating amount becomes excessively thick, so the temperature is cooled to 560 ° C or lower.

【019】本発明法により加工品を溶融亜鉛めっきする
一つの方法としては、図5に示す方法がある。すなわ
ち、大気雰囲気の燃焼室6で加工品を加熱して、目的の
温度になったらシャッタ−7を開いて、コンベア8、9
で還元性ガス供給管10を備えた間接加熱方式の還元室
11に移送し、そこで還元性ガスを供給しながら還元す
る。
One method for hot dip galvanizing a processed product by the method of the present invention is the method shown in FIG. That is, the processed product is heated in the combustion chamber 6 in the air atmosphere, and when the target temperature is reached, the shutter 7 is opened and the conveyors 8 and 9 are opened.
Then, it is transferred to the indirect heating type reduction chamber 11 provided with the reducing gas supply pipe 10, and is reduced there while supplying the reducing gas.

【020】還元が完了したなら、シャッタ−12を開
き、再びコンベア9、13で不活性ガス供給管14を備
えた冷却室15に移送して、めっき適性温度に調整し、
亜鉛めっき浴16に浸漬する。亜鉛めっき浴16への浸
漬は、冷却室15に連続してシャッタ−17で仕切られ
た密閉型のめっき室18を設けて、その内部にクレ−ン
19を配置し、このクレ−ン19で吊しながら行う。な
お、亜鉛めっき浴16よりの蒸発亜鉛によるめっき室1
8の汚染を防止するため、亜鉛めっき浴16にはAlを
0.05〜0.2%添加して、亜鉛の蒸発を防止するのが
好ましい。
When the reduction is completed, the shutter 12 is opened, the conveyer 9 and 13 are transferred again to the cooling chamber 15 equipped with the inert gas supply pipe 14, and the temperature suitable for plating is adjusted.
Immerse in the galvanizing bath 16. For immersion in the galvanizing bath 16, a cooling chamber 15 is provided with a closed type plating chamber 18 which is partitioned by a shutter 17, and a crane 19 is arranged inside the chamber. Do it while hanging. In addition, the plating chamber 1 using zinc evaporated from the zinc plating bath 16
In order to prevent the contamination of No. 8, Al is preferably added to the zinc plating bath 16 in an amount of 0.05 to 0.2% to prevent the evaporation of zinc.

【021】また、他の方法としては、図5の各室の仕切
りをシャッタ−の代わりに図6に示すように各室の間に
不活性ガスカ−テン形成可能な不活性ガス供給管14を
備えた置換室20を配置して、燃焼室6からめっき室1
8に至るまで1本のコンベア21を通す構造にし、加工
品をめっき室18から亜鉛めっき浴16に投入し、めっ
き後の加工品をコンベア式引き上げ機22で取り出すよ
うにしてもよい。
As another method, instead of a shutter for partitioning each chamber in FIG. 5, an inert gas supply pipe 14 capable of forming an inert gas caten between the chambers as shown in FIG. 6 is used. The replacement chamber 20 provided is arranged to move from the combustion chamber 6 to the plating chamber 1
It is also possible to have a structure in which one conveyor 21 is passed up to 8 and the processed product is put into the galvanizing bath 16 from the plating chamber 18 and the processed product after plating is taken out by the conveyor type pulling machine 22.

【022】[0222]

【実施例】【Example】

実施例1 図4に示す実験装置で円筒1の内部を大気雰囲気にし
て、機械油と白色塗料を塗布した肉厚2.3mm、長さ
20cm、5cm角の黒錆だけの熱延鋼板製コラム(黒
錆厚み7.2μm)を420℃で3分間加熱して、付着
物を焼却した後、円筒1を窒素ガスパ−ジして、水素濃
度24.2%のH2−N2混合ガスを導入し、420℃に
加熱しながら160秒間還元した。還元が完了したなら
直ちに浴温450℃の亜鉛めっき浴5に落下させて、3
0秒間浸漬した。このコラムを亜鉛めっき浴5より引き
上げ後表面を観察したが、不めっきは認められなかっ
た。
Example 1 In the experimental apparatus shown in FIG. 4, the inside of the cylinder 1 was placed in the atmosphere, and machine oil and white paint were applied to the column made of hot-rolled steel sheet with a thickness of 2.3 mm, a length of 20 cm, and a 5 cm square, and only black rust. (Black rust thickness 7.2 μm) is heated at 420 ° C. for 3 minutes to incinerate the adhered substances, and then the cylinder 1 is purged with nitrogen gas to generate a H 2 —N 2 mixed gas having a hydrogen concentration of 24.2%. It was introduced and reduced for 160 seconds while heating to 420 ° C. When the reduction is completed, immediately drop it in the zinc plating bath 5 with a bath temperature of 450 ° C.
It was immersed for 0 seconds. After pulling up this column from the zinc plating bath 5, the surface was observed, but no non-plating was observed.

【023】実施例2 実施例1と同様のコラムを屋外に放置して、全表面積の
約42%に赤錆を発生させ、これに機械油と白色塗料を
塗布して、実施例1と同要領で図4の実験装置で溶融亜
鉛めっきを施した。円筒1での加熱は、250℃の大気
雰囲気中で5分間行い、加熱後の還元は、760℃の水
素濃度4.3%のH2−N2混合ガスで120秒間行っ
た。そして、還元後は、赤外線炉4による加熱を中止し
て、443℃まで冷却し、浴温450℃の亜鉛めっき浴
5に落下させて、30秒間浸漬した。このコラムも亜鉛
めっき浴5より引き上げ後表面を観察したが、不めっき
は認められなかった。 比較例 実施例2において、大気雰囲気中でのコラム加熱を省略
して溶融亜鉛めっきを施したが、機械油と白色塗料の塗
布部分に不めっきが発生した。
Example 2 A column similar to that of Example 1 was left outdoors to cause red rust to occur on about 42% of the total surface area, and mechanical oil and white paint were applied to this, and the same procedure as in Example 1 was performed. Then, hot dip galvanizing was performed using the experimental apparatus shown in FIG. The heating in the cylinder 1 was carried out for 5 minutes in the air atmosphere at 250 ° C., and the reduction after the heating was carried out for 120 seconds in the H 2 —N 2 mixed gas having a hydrogen concentration of 4.3% at 760 ° C. After the reduction, heating by the infrared furnace 4 was stopped, the temperature was cooled to 443 ° C., and the zinc plating bath 5 having a bath temperature of 450 ° C. was dropped and immersed for 30 seconds. The surface of this column was also lifted from the zinc plating bath 5 and the surface was observed, but no plating was observed. Comparative Example In Example 2, hot-dip galvanizing was performed by omitting column heating in the air atmosphere, but non-plating occurred in the portion where the machine oil and the white paint were applied.

【024】[0242]

【発明の効果】以上のように、本発明の溶融亜鉛めっき
方法は、湿式前処理ではなく、乾式前処理であるので、
作業環境や作業条件を著しく改善できる。
As described above, since the hot dip galvanizing method of the present invention is not a wet pretreatment but a dry pretreatment,
The working environment and working conditions can be significantly improved.

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

【図1】黒皮の低炭素熱延鋼板を水素ガスと窒素ガスの
混合ガス中にて500℃で還元した場合の水素ガス濃度
と還元時間による溶融亜鉛めっき性を示したプロット図
である。
FIG. 1 is a plot diagram showing the hot dip galvanizability depending on the hydrogen gas concentration and the reduction time when a black-skinned low carbon hot-rolled steel sheet is reduced at 500 ° C. in a mixed gas of hydrogen gas and nitrogen gas.

【図2】黒皮の低炭素熱延鋼板を水素ガスと窒素ガスの
混合ガス中にて600℃で還元した場合の水素ガス濃度
と還元時間による溶融亜鉛めっき性を示したプロット図
である。
FIG. 2 is a plot diagram showing hot-dip galvanizability according to hydrogen gas concentration and reduction time when a black skin low carbon hot-rolled steel sheet is reduced at 600 ° C. in a mixed gas of hydrogen gas and nitrogen gas.

【図3】黒錆の酸化による赤錆の発生した低炭素熱延鋼
板を水素ガスと窒素ガスの混合ガス中にて500℃で還
元した場合の水素ガス濃度と還元時間による溶融亜鉛め
っき性を示したプロット図である。
FIG. 3 shows hot dip galvanizability depending on hydrogen gas concentration and reduction time when a low carbon hot-rolled steel sheet in which red rust caused by oxidation of black rust is reduced in a mixed gas of hydrogen gas and nitrogen gas at 500 ° C. FIG.

【図4】熱延鋼板の溶融亜鉛めっきの実験に使用したガ
ス還元方式の実験装置の概略図である。
FIG. 4 is a schematic diagram of a gas reduction type experimental apparatus used for an experiment of hot-dip galvanizing a hot-rolled steel sheet.

【図5】本発明法により加工品を工業的に溶融亜鉛めっ
きする場合のめっき装置概略図である。
FIG. 5 is a schematic diagram of a plating apparatus for industrially hot-dip galvanizing a processed product by the method of the present invention.

【図6】本発明法により加工品を工業的に溶融亜鉛めっ
きする場合の他のめっき装置概略図である。
FIG. 6 is a schematic view of another plating apparatus for industrially hot-dip galvanizing a processed product by the method of the present invention.

【符号の説明】[Explanation of symbols]

1…円筒、2…試験片保持棒、3…試験片、4…赤外線
炉、5…亜鉛めっき浴、6…燃焼室、7…シャッタ−、
8、9…コンベア、10…還元性ガス供給管、11…還
元室、12…シャッタ−、13…コンベア、14…不活
性ガス供給管、15…冷却室、16…亜鉛めっき浴、1
7…シャッタ−、18…めっき室、19…クレ−ン、2
0…置換室、21…コンベア、22…コンベア式引き上
げ機、
1 ... Cylinder, 2 ... Test piece holding rod, 3 ... Test piece, 4 ... Infrared furnace, 5 ... Zinc plating bath, 6 ... Combustion chamber, 7 ... Shutter,
8, 9 ... Conveyor, 10 ... Reducing gas supply pipe, 11 ... Reduction chamber, 12 ... Shutter, 13 ... Conveyor, 14 ... Inert gas supply pipe, 15 ... Cooling chamber, 16 ... Zinc plating bath, 1
7 ... Shutter, 18 ... Plating chamber, 19 ... Crane, 2
0 ... Substitution chamber, 21 ... Conveyor, 22 ... Conveyor type pulling machine,

───────────────────────────────────────────────────── フロントページの続き (72)発明者 中村 一郎 千葉県八千代市大和田新田672番地の1 新星鋼業株式会社内 (72)発明者 前北 杲彦 千葉県八千代市大和田新田672番地の1 新星鋼業株式会社内 (72)発明者 伊藤 修一 千葉県八千代市大和田新田672番地の1 新星鋼業株式会社内 (72)発明者 阿部 信浩 愛知県名古屋市瑞穂区二野町7番21号 株 式会社エステム内 (72)発明者 首藤 治三 大阪府大阪市住之江区北加賀屋三丁目3番 44号 オ−エム工業株式会社内 (72)発明者 長尾 隆 愛知県名古屋市瑞穂区二野町7番21号 株 式会社エステム内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Ichiro Nakamura 1 at 672 Owada Nitta, Yachiyo-shi, Chiba Shinsei Kogyo Co., Ltd. (72) Inventor Masuhiko Maekita, 672 Owada Nitta, Yachiyo-shi, Chiba 1 Within Nova Steel Industry Co., Ltd. (72) Inventor Shuichi Ito 672 Owada Nitta, Yachiyo City, Chiba Prefecture Within Nova Steel Industry Co., Ltd. (72) Inventor Nobuhiro Abe 7-21 Ninomachi, Mizuho-ku, Nagoya City, Aichi Prefecture No. Incorporated company Estem (72) Inventor Jitsuzo Suto 3-3-44 Kitakagaya, Suminoe-ku, Osaka City, Osaka Prefecture O-M Industrial Co., Ltd. (72) Inventor Takashi Nagao Nino, Mizuho-ku, Aichi Prefecture 7-21 Machi Incorporated company Estem

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 熱延酸化スケ−ル付着鉄鋼加工品に前
処理を施した後、430〜530℃の溶融亜鉛めっき浴
に浸漬してめっきし、その後、めっき浴より取り出し
て、過剰の付着亜鉛を除去する溶融亜鉛めっき方法にお
いて、前記前処理を、加工品を酸化性雰囲気中で加熱し
て、付着物を燃焼させた後、還元性ガス雰囲気中にて4
00〜800℃で還元し、その後、非酸化性ガス雰囲気
中で560℃以下になるように温度調整する方法で行う
ことを特徴とする酸化スケ−ル付着鉄鋼加工品の溶融亜
鉛めっき方法。
1. A hot-rolled oxide scale-adhered steel product is pretreated, then immersed in a hot dip galvanizing bath at 430 to 530 ° C. for plating, and then taken out from the plating bath and excessively adhered. In the hot dip galvanizing method for removing zinc, the pretreatment is performed by heating the processed product in an oxidizing atmosphere to burn the deposits, and then in a reducing gas atmosphere.
A hot dip galvanizing method for a steel product on which an oxide scale is attached, which is carried out by a method of reducing at 00 to 800 ° C. and then adjusting the temperature so as to be 560 ° C. or less in a non-oxidizing gas atmosphere.
【請求項2】 還元性ガスとして、水素濃度2〜10
0%、残部が窒素ガスからなるガスを用いることを特徴
とする請求項1に記載の酸化スケ−ル付着鉄鋼加工品の
溶融亜鉛めっき方法。
2. A hydrogen concentration of 2 to 10 as the reducing gas.
The hot-dip galvanizing method for a steel product with an attached oxide scale according to claim 1, wherein a gas consisting of 0% and the balance being nitrogen gas is used.
【請求項3】 加工品を還元性ガス雰囲気中で還元す
る前に予熱することを特徴とする請求項1に記載の酸化
スケ−ル付着鉄鋼加工品の溶融亜鉛めっき方法。
3. The hot dip galvanizing method for a steel oxide-fabricated steel workpiece according to claim 1, wherein the workpiece is preheated before being reduced in a reducing gas atmosphere.
JP25566092A 1992-08-31 1992-08-31 Hot-dip galvanizing method for steel products with oxide scale attached Expired - Lifetime JP2611175B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP25566092A JP2611175B2 (en) 1992-08-31 1992-08-31 Hot-dip galvanizing method for steel products with oxide scale attached

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP25566092A JP2611175B2 (en) 1992-08-31 1992-08-31 Hot-dip galvanizing method for steel products with oxide scale attached

Publications (2)

Publication Number Publication Date
JPH0681097A true JPH0681097A (en) 1994-03-22
JP2611175B2 JP2611175B2 (en) 1997-05-21

Family

ID=17281843

Family Applications (1)

Application Number Title Priority Date Filing Date
JP25566092A Expired - Lifetime JP2611175B2 (en) 1992-08-31 1992-08-31 Hot-dip galvanizing method for steel products with oxide scale attached

Country Status (1)

Country Link
JP (1) JP2611175B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR19990057390A (en) * 1997-12-29 1999-07-15 이구택 Process for producing acid-free alloyed hot-dip galvanized hot rolled steel sheet with excellent powder resistance and surface quality
JP2007332415A (en) * 2006-06-14 2007-12-27 Jfe Steel Kk Method for manufacturing hot-dip galvanized steel sheet
JP2013007066A (en) * 2011-06-22 2013-01-10 Mitsubishi Cable Ind Ltd Method and device for producing plated wire material

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR19990057390A (en) * 1997-12-29 1999-07-15 이구택 Process for producing acid-free alloyed hot-dip galvanized hot rolled steel sheet with excellent powder resistance and surface quality
JP2007332415A (en) * 2006-06-14 2007-12-27 Jfe Steel Kk Method for manufacturing hot-dip galvanized steel sheet
JP2013007066A (en) * 2011-06-22 2013-01-10 Mitsubishi Cable Ind Ltd Method and device for producing plated wire material

Also Published As

Publication number Publication date
JP2611175B2 (en) 1997-05-21

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