JPH0949073A - Formation of magnesium vapor-deposited layer or zine vapor-deposited layer under controlled granular vapor-deposited substance - Google Patents

Formation of magnesium vapor-deposited layer or zine vapor-deposited layer under controlled granular vapor-deposited substance

Info

Publication number
JPH0949073A
JPH0949073A JP22265395A JP22265395A JPH0949073A JP H0949073 A JPH0949073 A JP H0949073A JP 22265395 A JP22265395 A JP 22265395A JP 22265395 A JP22265395 A JP 22265395A JP H0949073 A JPH0949073 A JP H0949073A
Authority
JP
Japan
Prior art keywords
vapor
deposited
duct
deposited layer
flow rate
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.)
Withdrawn
Application number
JP22265395A
Other languages
Japanese (ja)
Inventor
Yasushi Fukui
康 福居
Tadaaki Miono
忠昭 三尾野
Minoru Saito
実 斎藤
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.)
Nippon Steel Nisshin Co Ltd
Original Assignee
Nisshin Steel Co Ltd
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 Nisshin Steel Co Ltd filed Critical Nisshin Steel Co Ltd
Priority to JP22265395A priority Critical patent/JPH0949073A/en
Publication of JPH0949073A publication Critical patent/JPH0949073A/en
Withdrawn legal-status Critical Current

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  • Physical Vapour Deposition (AREA)

Abstract

PROBLEM TO BE SOLVED: To suppress the formation of a granular vapor-deposited substance and to prepare a sound plating layer by vapor deposition. SOLUTION: When vapor of a metal to be vapor-deposited is transferred from an evaporation tank 5 to a substrate (steel strip 13) to be subjected to vapor deposition, the flow rate of vapor passing through the outlet of a duct 12 near the substrate is regulated to <=55g/sec.m<2> in the case of Mg and <=220g/ sec.m<2> in the case of Zn. Since the flow rate of vapor at the outlet of the duct is regulated, the formation of a granular vapor-deposited substance is suppressed and a plating layer free from defects due to the granular vapor- deposited substance is formed by vapor deposition.

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、ダクトを介して蒸気を
輸送したMg又はZnを基板上に高速蒸着する方法に関
する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for high-speed vapor deposition of Mg or Zn, which carries vapor through a duct.

【0002】[0002]

【従来の技術】Zn−Mg等のMg含有めっき鋼板は、
従来の表面処理鋼板と比較して非常に優れた耐食性を示
すことから、過酷な腐食雰囲気に曝される構造材等とし
て今後の用途展開が期待されている。めっき層に取り込
まれるMgは、蒸発槽で発生させたMg蒸気をめっき原
板の表面に送り込んで蒸着させている。真空中で液相が
存在するZn等の金属を蒸発させる場合、たとえば図1
に示す設備構成をもつ装置が使用される[日新技報第5
6号(1987)第41頁]。この装置では、被蒸発金
属源を溶解炉1で溶解し、融液2を用意する。融液2
は、シュノーケル3を経て、真空槽4内に配置されてい
る蒸発槽5に送り込まれる。融液2は、蒸発槽5内でヒ
ータ6により加熱され蒸気となる。
2. Description of the Related Art Mg-containing plated steel sheets such as Zn-Mg are
Since it shows extremely excellent corrosion resistance compared to conventional surface-treated steel sheets, future application development is expected as a structural material exposed to a severe corrosive atmosphere. The Mg taken into the plating layer is vaporized by sending Mg vapor generated in the evaporation tank to the surface of the original plating plate. When evaporating a metal such as Zn having a liquid phase in a vacuum, for example, as shown in FIG.
A device having the equipment configuration shown in is used [Nissin Technical Report No. 5
6 (1987), page 41]. In this apparatus, a source of metal to be evaporated is melted in a melting furnace 1 to prepare a melt 2. Melt 2
Is sent to the evaporation tank 5 arranged in the vacuum tank 4 via the snorkel 3. The melt 2 is heated by the heater 6 in the evaporation tank 5 and becomes vapor.

【0003】金属蒸気は、フード7に案内されて鋼板等
の被蒸着物に到達し、被蒸着物の表面に蒸着される。こ
のとき、金属蒸気の流量は、蒸発槽5の出側に設けられ
ているシャッター8の開度を調節することにより制御さ
れる。また、本発明者等は、ZnやMgを蒸発させる装
置として、図2に示す構造の蒸発装置を特願平6−25
4829号で提案した。この装置においては、蒸発槽5
にMg,Zn等の蒸着金属9を収容したルツボ10を配
置し、ヒータ6で蒸着金属9を加熱する。蒸発したMg
又はZnの蒸気は、シャッター8で流量が調整され、円
形ダクト11から矩形ダクト12を経て、鋼帯13に蒸
着される。この方法では、蒸発槽5で発生した蒸気のほ
とんどが基板である鋼帯13に蒸着し、基板に蒸着せず
無効になる蒸気が少ない。そのため、真空槽内の汚染が
少なく、メンテナンスが容易になる。
The metal vapor is guided by the hood 7 to reach an object to be vapor-deposited such as a steel plate, and is vapor-deposited on the surface of the object to be vapor-deposited. At this time, the flow rate of the metal vapor is controlled by adjusting the opening degree of the shutter 8 provided on the outlet side of the evaporation tank 5. Further, the inventors of the present invention have proposed an evaporator having a structure shown in FIG. 2 as an apparatus for evaporating Zn and Mg.
Proposed in No. 4829. In this device, the evaporation tank 5
A crucible 10 accommodating a vapor-deposited metal 9 such as Mg or Zn is placed in the chamber, and the heater 6 heats the vapor-deposited metal 9. Evaporated Mg
Alternatively, the flow rate of Zn vapor is adjusted by the shutter 8 and is deposited on the steel strip 13 from the circular duct 11 through the rectangular duct 12. In this method, most of the vapor generated in the evaporation tank 5 is vapor-deposited on the steel strip 13 which is the substrate, and the vapor that is not vaporized on the substrate and is ineffective is small. Therefore, the inside of the vacuum chamber is less contaminated and the maintenance becomes easier.

【0004】[0004]

【発明が解決しようとする課題】ダクトで輸送した蒸気
を基板上に蒸着させる方法は、非常に効率のよい方法で
ある。しかし、1トール以下の真空度では、ダクト内を
通過する蒸気量が多くなると1μmから数mmの粒子状
蒸着物が付着する場合がある。蒸着層の厚みは0.1〜
10μmの範囲にある場合が多いため、粒径の大きな蒸
着物は、蒸着膜の欠陥となる。めっき鋼板の場合、数十
μmから数mmの蒸着物は、外観不良やプレス加工不良
の原因となり、商品として出荷できない。また、数μm
の蒸着物であっても、プレス等の加工を受けたとき、脱
落して下地鋼を露出させ、耐食性を劣化させる。合金め
っきを施した場合では、粒子状の蒸着物がある部分は、
濃度が他の部分と異なるため電気化学的作用によって耐
食性が低下する。特に、大量の粒子状蒸着物が付着した
場合には、耐食性が大きく劣化する。
The method of depositing the vapor transported by the duct on the substrate is a very efficient method. However, at a degree of vacuum of 1 Torr or less, if the amount of vapor passing through the duct increases, a particulate deposit of 1 μm to several mm may adhere. The thickness of the deposited layer is 0.1
Since it is often in the range of 10 μm, a deposit having a large grain size becomes a defect of the deposited film. In the case of a plated steel sheet, a deposit of several tens of μm to several mm causes defective appearance and defective press working, and cannot be shipped as a product. Also, several μm
Even when it is subjected to processing such as pressing, even the vapor-deposited product of (1) falls off to expose the base steel and deteriorate the corrosion resistance. When alloy plating is applied, the part where there is a particulate deposit is
Since the concentration is different from the other parts, the corrosion resistance is reduced by the electrochemical action. In particular, when a large amount of particulate deposit is attached, the corrosion resistance is greatly deteriorated.

【0005】粒子状の蒸着物は、ダクト出口における蒸
気の流れ方向,被蒸着物による蒸気の冷却、雰囲気ガス
による冷却等の要因が複雑に絡んで発生する。そのた
め、条件制御が困難であり、粒子状蒸着物の生成を防止
する有効な方法がこれまで提案されていない。本発明
は、このような問題を解消すべく案出されたものであ
り、ダクト出口における蒸気の流量を制御することによ
り、粒子状蒸着物の生成を効果的に防止し、高品質の蒸
着めっき層を形成することを目的とする。
[0005] The particulate vapor deposition material is complicatedly entangled with factors such as the flow direction of vapor at the outlet of the duct, the vapor cooling by the vapor deposition material, and the cooling by the atmospheric gas. Therefore, it is difficult to control the conditions, and an effective method for preventing the formation of particulate deposits has not been proposed so far. The present invention has been devised to solve such a problem, and by controlling the flow rate of vapor at the duct outlet, it is possible to effectively prevent the formation of particulate deposits and to achieve high-quality vapor deposition plating. The purpose is to form a layer.

【0006】[0006]

【課題を解決するための手段】本発明の蒸着層形成方法
は、その目的を達成するため、蒸発槽から被蒸着基板に
蒸着金属の蒸気を輸送する際、被蒸着基板近傍のダクト
出口を通過する蒸気の流量をMgでは55g/秒・m2
以下に、Znでは220g/秒・m2 以下に規制するこ
とを特徴とする。
In order to achieve the object, the vapor deposition layer forming method of the present invention, when transporting vapor of vapor deposition metal from an evaporation tank to a vapor deposition substrate, passes through a duct outlet near the vapor deposition substrate. The flow rate of steam is 55 g / sec · m 2 for Mg.
In the following, Zn is regulated to 220 g / sec · m 2 or less.

【0007】[0007]

【作用】本発明者等は、蒸着めっき層に取り込まれる粒
子状蒸着物の生成過程について種々調査検討した。その
結果、ダクト出口を通過する蒸気の流量が粒子状蒸着物
の生成に大きな影響を及ぼしていることを知見した。蒸
気流量が多くなると、ダクト内の圧力が高まり、ダクト
出口での断熱膨張が大きくなる。また、蒸気流量が多く
なった場合、被蒸着物とダクト出口との間でも局部的に
圧力が高い状態になり、真空中でも被蒸着物との熱交換
によって蒸気が冷却され易くなる。その結果、蒸気温度
が低下し、粒子状蒸着物が発生するものと推察される。
そして、種々の実験結果から、ダクト出口を通過する蒸
気の流量をMgでは55g/秒・m2 以下に、Znでは
220g/秒・m2 以下に下げることによって、断熱膨
張や蒸気の冷却が生じた場合であっても粒子状蒸着物の
発生が抑制されることを見い出した。ダクト出口におけ
る蒸気の流量規制は、ダクトの途中で断面積変化に起因
する蒸気流量の変動による影響を受けず、基板上に形成
される蒸着めっき層に粒子状蒸着物が取り込まれること
を防止する。その結果、得られた蒸着めっき層は、粒子
状蒸着物に起因する欠陥がなく、高品質のめっき層とな
る。これに対し、ダクト出口を通過する蒸気の流量が、
Mgで55g/秒・m2 ,Znで220g/秒・m2
超えると、後述する実施例で説明するように得られた蒸
着層に粒子状蒸着物が取り込まれることが避けられな
い。
The present inventors conducted various investigations on the formation process of particulate deposits taken into the vapor deposition plating layer. As a result, it was found that the flow rate of the vapor passing through the duct outlet had a great influence on the formation of the particulate deposit. When the steam flow rate increases, the pressure inside the duct increases, and the adiabatic expansion at the duct outlet increases. Further, when the vapor flow rate increases, the pressure is locally high between the deposition target and the duct outlet, and the vapor is easily cooled by heat exchange with the deposition target even in a vacuum. As a result, the vapor temperature is lowered, and it is speculated that particulate deposits are generated.
From various experimental results, by lowering the flow rate of steam passing through the duct outlet to 55 g / sec · m 2 or less for Mg and 220 g / sec · m 2 or less for Zn, adiabatic expansion and cooling of steam occur. It has been found that even in the case of occurrence, the generation of particulate deposition is suppressed. The regulation of the flow rate of steam at the duct outlet is not affected by the fluctuation of the steam flow rate due to the change in the cross-sectional area in the middle of the duct, and prevents the particulate deposition material from being taken into the deposition plating layer formed on the substrate. . As a result, the obtained vapor-deposited plated layer is a high-quality plated layer without defects due to the particulate deposit. On the other hand, the flow rate of steam passing through the duct outlet is
When the Mg content exceeds 55 g / sec · m 2 and the Zn content exceeds 220 g / sec · m 2 , it is inevitable that the particulate deposit is taken into the vapor deposition layer obtained as described in Examples below.

【0008】[0008]

【実施例】図2に示した設備構成の装置を使用してMg
及びZnを蒸発させた。蒸発槽5は、直径800mmの
鉄製ルツボ10を収容しており、発生した蒸気を上部に
設けたダクト11,12で走行中の鋼帯13まで輸送す
る。装置全体は真空チャンバ内に設置されており、鋼帯
13の払出し,巻取り用のリールやデフレクタロール等
のロール類が同一の真空チャンバ又は連結された真空チ
ャンバに配置されているが、図1ではロール類の図示を
省略した。ダクトの断面形状は、途中まで円形状であ
り、鋼帯13の近傍で板幅方向に関して蒸気が均一に輸
送されるように矩形状になっている。すなわち、断面積
502400mm2 の円形ダクト11の先端に、300
mm×80mmの矩形ダクト12を接続した。
EXAMPLE Using the apparatus having the equipment configuration shown in FIG.
And Zn were evaporated. The evaporation tank 5 accommodates an iron crucible 10 having a diameter of 800 mm, and transports the generated steam to the running steel strip 13 through ducts 11 and 12 provided at the upper part. The entire apparatus is installed in a vacuum chamber, and rolls such as reels and deflector rolls for paying out and winding the steel strip 13 are arranged in the same vacuum chamber or a connected vacuum chamber. Then, illustration of rolls is omitted. The cross-sectional shape of the duct is circular until halfway, and is rectangular in the vicinity of the steel strip 13 so that steam is uniformly transported in the plate width direction. That is, at the tip of the circular duct 11 having a cross-sectional area of 502400 mm 2 ,
A rectangular duct 12 of mm × 80 mm was connected.

【0009】円形ダクト11の曲がり部にシャッタ8を
設けた。ダクトを通過する蒸気の流量は、シャッタ8の
開度調整及びルツボ10の温度調整によって制御した。
ダクトは、蒸気の付着を防止するためMg蒸着では65
0℃,Zn蒸着では550℃に加熱した。ポンプによっ
て排気しながら窒素を導入し、真空チャンバ内を0.0
03〜0.5トールの減圧雰囲気に維持した状態で、ダ
クト13出口における蒸気流量を変えながらMg及びZ
nを鋼帯13に蒸着させた。得られた蒸着めっき鋼板の
表面をSEMで観察し、粒子状蒸着物の個数をカウント
した。個数を単位面積当りの個数として算出した。な
お、めっき層の厚さは、鋼板の送り速度を調整すること
により常に1μmとなるように設定した。
The shutter 8 is provided at the curved portion of the circular duct 11. The flow rate of steam passing through the duct was controlled by adjusting the opening of the shutter 8 and the temperature of the crucible 10.
The duct is 65 for Mg vapor deposition to prevent vapor deposition.
It was heated to 0 ° C. and 550 ° C. for Zn vapor deposition. Nitrogen is introduced while exhausting with a pump, and the inside of the vacuum chamber is 0.0
While maintaining a reduced pressure atmosphere of 03 to 0.5 Torr, Mg and Z while changing the steam flow rate at the outlet of the duct 13
n was vapor-deposited on the steel strip 13. The surface of the obtained vapor-deposited plated steel sheet was observed by SEM, and the number of particulate vapor deposits was counted. The number was calculated as the number per unit area. The thickness of the plating layer was set so as to always be 1 μm by adjusting the feed rate of the steel sheet.

【0010】表1及び表2は、以上のようにして求めら
れた粒子状蒸着物発生個数をダクト13出口における蒸
気流量で整理した表である。表1から明らかなように、
Mg蒸着ではダクト13の出口を通過するMg蒸気の流
量を55g/秒・m2 以下に規制することにより、粒子
状蒸着物を含まない蒸着めっき層が形成されることが確
認された。また、Zn蒸着では、表2から明らかなよう
にZn蒸気の流量を220g/秒・m2 以下に規制する
ことにより、粒子状蒸着物を含まない蒸着めっき層が形
成されることが確認された。
Tables 1 and 2 are tables in which the number of generated particulate deposits obtained as described above is arranged by the vapor flow rate at the outlet of the duct 13. As is clear from Table 1,
In the Mg deposition, it was confirmed that the deposition plating layer containing no particulate deposition was formed by limiting the flow rate of Mg vapor passing through the outlet of the duct 13 to 55 g / sec · m 2 or less. Further, in Zn vapor deposition, as is clear from Table 2, it was confirmed that the vapor deposition plating layer containing no particulate vapor deposition was formed by regulating the flow rate of Zn vapor to 220 g / sec · m 2 or less. .

【0011】 [0011]

【0012】 [0012]

【0013】[0013]

【発明の効果】以上に説明したように、本発明において
は、蒸発槽から基材に送られる蒸着金属の蒸気が基材近
傍に開口したダクトの出口を通過する流量を規制するこ
とにより、粒子状蒸着物の生成を抑制し、粒子状蒸着物
に起因する欠陥のない健全な蒸着層を形成している。こ
のようにして蒸着めっきされた鋼板等は、本来の蒸着Z
nめっき層又は蒸着Mgめっき層がもつ高耐食性を十分
に活かし、各種分野で使用される。
As described above, according to the present invention, by controlling the flow rate of vapor of vapor-deposited metal sent from the evaporation tank to the substrate through the outlet of the duct opened in the vicinity of the substrate, The formation of particulate vapor deposits is suppressed, and a sound vapor deposition layer having no defects caused by the particulate vapor deposits is formed. The steel plate etc. plated by vapor deposition in this way are
It is used in various fields by fully utilizing the high corrosion resistance of the n-plated layer or the evaporated Mg-plated layer.

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

【図1】 蒸着めっきに使用される従来の金属蒸発装置FIG. 1 Conventional metal vaporizer used for vapor deposition plating

【図2】 本発明者等が先に提案したダクトを使用した
蒸発装置
FIG. 2 is an evaporator using a duct previously proposed by the present inventors.

【符号の説明】[Explanation of symbols]

1:溶解炉 2:融液 3:シュノーケル 4:
真空槽 5:蒸発槽 6:ヒータ 7:フード 8:シャッタ 9:蒸
着金属(Mg又はZn) 10:ルツボ 11:円形ダクト 12:矩形ダク
ト 13:鋼帯
1: Melting furnace 2: Melt 3: Snorkel 4:
Vacuum tank 5: Evaporation tank 6: Heater 7: Hood 8: Shutter 9: Evaporated metal (Mg or Zn) 10: Crucible 11: Circular duct 12: Rectangular duct 13: Steel strip

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 蒸発槽から被蒸着基板に蒸着金属である
Mg蒸気を輸送する際、被蒸着基板近傍のダクト出口を
通過するMg蒸気の流量を55g/秒・m2以下に規制
することを特徴とする粒子状蒸着物を抑制したMg蒸着
層又はZn蒸着層の形成方法。
1. When transporting Mg vapor, which is a vapor deposition metal, from an evaporation tank to a vapor deposition substrate, the flow rate of Mg vapor passing through a duct outlet near the vapor deposition substrate is regulated to 55 g / sec · m 2 or less. A method for forming a Mg vapor-deposited layer or a Zn vapor-deposited layer which suppresses the characteristic particulate deposit.
【請求項2】 蒸発槽から被蒸着基板に蒸着金属である
Zn蒸気を輸送する際、被蒸着基板近傍のダクト出口を
通過するZn蒸気の流量を220g/秒・m2 以下に規
制することを特徴とする粒子状蒸着物を抑制したMg蒸
着層又はZn蒸着層の形成方法。
2. When transporting Zn vapor, which is vapor-deposited metal, from the evaporation tank to the vapor-deposited substrate, the flow rate of Zn vapor passing through the duct outlet near the vapor-deposited substrate is regulated to 220 g / sec · m 2 or less. A method for forming a Mg vapor-deposited layer or a Zn vapor-deposited layer which suppresses the characteristic particulate deposit.
JP22265395A 1995-08-08 1995-08-08 Formation of magnesium vapor-deposited layer or zine vapor-deposited layer under controlled granular vapor-deposited substance Withdrawn JPH0949073A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22265395A JPH0949073A (en) 1995-08-08 1995-08-08 Formation of magnesium vapor-deposited layer or zine vapor-deposited layer under controlled granular vapor-deposited substance

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22265395A JPH0949073A (en) 1995-08-08 1995-08-08 Formation of magnesium vapor-deposited layer or zine vapor-deposited layer under controlled granular vapor-deposited substance

Publications (1)

Publication Number Publication Date
JPH0949073A true JPH0949073A (en) 1997-02-18

Family

ID=16785830

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22265395A Withdrawn JPH0949073A (en) 1995-08-08 1995-08-08 Formation of magnesium vapor-deposited layer or zine vapor-deposited layer under controlled granular vapor-deposited substance

Country Status (1)

Country Link
JP (1) JPH0949073A (en)

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