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JPH0573837B2 - - Google Patents
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JPH0573837B2 - - Google Patents

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Publication number
JPH0573837B2
JPH0573837B2 JP60266086A JP26608685A JPH0573837B2 JP H0573837 B2 JPH0573837 B2 JP H0573837B2 JP 60266086 A JP60266086 A JP 60266086A JP 26608685 A JP26608685 A JP 26608685A JP H0573837 B2 JPH0573837 B2 JP H0573837B2
Authority
JP
Japan
Prior art keywords
plating
bath
seconds
energization
present
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 - Fee Related
Application number
JP60266086A
Other languages
Japanese (ja)
Other versions
JPS62127493A (en
Inventor
Shigeki Matsumoto
Daiji Tonai
Yoichi Nakano
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.)
Sumitomo Metal Mining Co Ltd
Original Assignee
Sumitomo Metal Mining 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 Sumitomo Metal Mining Co Ltd filed Critical Sumitomo Metal Mining Co Ltd
Priority to JP26608685A priority Critical patent/JPS62127493A/en
Publication of JPS62127493A publication Critical patent/JPS62127493A/en
Publication of JPH0573837B2 publication Critical patent/JPH0573837B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Electroplating And Plating Baths Therefor (AREA)
  • Electroplating Methods And Accessories (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、硫酸塩浴、硼弗化物浴等のメツキ浴
を用いる電気錫メツキ法の改善に関するものであ
る。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to an improvement in the electrolytic tin plating process using a plating bath such as a sulfate bath or a borofluoride bath.

〔従来の技術〕[Conventional technology]

電子部品の露出金属部には防錆及び半田付け性
を目的として電気錫メツキが施されている。この
錫メツキには通常硫酸塩浴、硼弗化物浴が用いら
れるが、このような錫メツキ浴によりメツキした
被膜はメツキ後数日してからホイスカーと称され
るヒゲ状の結晶が発生することがある。このよう
なホイスカーは電気回路の短絡等のトラブルを生
じるため極力抑制しなければならず、一般には特
殊な下地メツキを施したり、メツキ後に熱処理を
行うなどの方策が採られている。
Electrolytic tin plating is applied to the exposed metal parts of electronic components for the purpose of rust prevention and solderability. Usually, a sulfate bath or a borofluoride bath is used for this tin plating, but whisker-like crystals called whiskers occur in the film plated with such a tin plating bath several days after plating. There is. Such whiskers cause problems such as short circuits in electric circuits, so they must be suppressed as much as possible, and measures such as applying a special base plating or heat treatment after plating are generally taken.

ところで、上記電気錫メツキ法において、メツ
キ中にメツキ被膜表面に針状又は糸状の異常析出
が発生することがある。これはホイスカーとは異
なり、電着中に形成される多結晶体である。この
異常析出発生のメカニズムについてはいまだ明ら
かではないが、カソード表面の結晶構造、結晶の
異方成長性、化学親和力等が原因となつてデンド
ライト前駆体が生成し、この前駆体に局部的に高
電流密度の電流が流れ加速度的に成長するためと
考えられる。この異常析出は前記した錫メツキの
場合のホイスカーと同様に電気回路の短絡の原因
となり電子部品等の信頼性を損うので、これを確
実に防止することが信頼性確保の上からも、又メ
ツキ製品歩留り向上のためにも強く要請されてい
た。このような錫メツキにおける異常析出を防止
するために従来、被メツキ物の酸浸漬、電解脱脂
又は化学研磨等の前処理を施したり、下地メツキ
を施したりする方法が採られているが、作業工程
が増して製造工程が煩雑になる上、異常析出を必
ずしも十分に抑制することができていないのが実
状である。又、メツキ浴に光沢剤を添加して光沢
メツキとすればこの異常析出は防止できるが、無
光沢錫メツキ仕様にはこの方法を適用できない。
By the way, in the above-mentioned electrolytic tin plating method, needle-like or thread-like abnormal deposits may occur on the surface of the plating film during plating. Unlike whiskers, this is a polycrystalline body formed during electrodeposition. Although the mechanism of this abnormal precipitation is not yet clear, dendrite precursors are formed due to the crystal structure of the cathode surface, the anisotropic growth of crystals, chemical affinity, etc. This is thought to be because a current with a current density flows and grows at an accelerated rate. Similar to the whiskers in the case of tin plating, this abnormal precipitation causes short circuits in electrical circuits and impairs the reliability of electronic components, so it is important to prevent this from the standpoint of ensuring reliability. This was also strongly requested to improve the yield of Metsuki products. In order to prevent such abnormal precipitation during tin plating, conventional methods have been used to pre-treat the material to be plated, such as acid immersion, electrolytic degreasing, or chemical polishing, or to perform base plating. The actual situation is that the number of steps increases, making the manufacturing process complicated, and that abnormal precipitation cannot always be sufficiently suppressed. Furthermore, this abnormal precipitation can be prevented by adding a brightening agent to the plating bath to achieve bright plating, but this method cannot be applied to matte tin plating specifications.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

本発明の目的は、異常析出発生のトラブルを、
前処理、下地メツキ等の追加工程や光沢剤添加等
の手段によらずに解消し、安定的にかつ廉価に電
気錫メツキを行ない得る方法を提供することにあ
る。
The purpose of the present invention is to solve the trouble of abnormal precipitation,
The object of the present invention is to provide a method for stably and inexpensively performing electrolytic tin plating without requiring additional steps such as pre-treatment or base plating or adding brighteners.

〔問題点を解決するための手段〕 この目的を達成するため、本発明の方法は、硫
酸塩浴、硼弗化物浴等のメツキ浴を用いる電気錫
メツキ法において、通電を間欠的に停止せしめる
点に特徴がある。
[Means for solving the problem] In order to achieve this object, the method of the present invention involves intermittently stopping the current supply in an electro-tinning method using a plating bath such as a sulfate bath or a borofluoride bath. The points are distinctive.

本発明の方法において、メツキ形成の順方向の
通電と、該通電の停止を行う。通電および停止の
好ましい時間は、被メツキ物の材質、メツキ浴組
成、電流密度等により影響されるので一律には言
えないが、通常の電流密度である1.5A/dm2
おいては、通電が約80秒以下、より好ましくは20
〜60秒を一単位とし、通電の停止は3秒以上、よ
り好ましくは5〜20秒を一単位とする範囲であ
る。
In the method of the present invention, energization is carried out in the forward direction for plating formation, and the energization is stopped. The preferred time for energizing and stopping cannot be determined uniformly because it is affected by the material of the object to be plated, the composition of the plating bath, the current density, etc., but at a normal current density of 1.5 A/dm 2 , the energizing time is approx. 80 seconds or less, more preferably 20
One unit is ~60 seconds, and the energization is stopped for 3 seconds or more, more preferably 5 to 20 seconds.

異常析出防止の効果の点からすると通電の時間
は短い程、停止時間は長い程よいが、通電時間が
短か過ぎたり停止時間が長過ぎたりすると、メツ
キ形成の能率が低下し好ましくない。又、通電時
間が80秒を超えたり、停止時間が3秒未満と短か
過ぎると、異常析出を十分に防止することが困難
である。
From the point of view of the effect of preventing abnormal deposition, the shorter the energization time and the longer the stop time, the better; however, if the energization time is too short or the stop time is too long, the efficiency of plating formation will decrease, which is undesirable. Furthermore, if the current application time exceeds 80 seconds or the stop time is too short, such as less than 3 seconds, it is difficult to sufficiently prevent abnormal deposition.

上記のように通電を間欠的に停止させることに
よる電流波形は特に限定されず、例えば矩形波、
ステツプ波、三角波、鋸波など何れであつても良
い。
The current waveform caused by intermittent stopping of energization as described above is not particularly limited, and for example, a rectangular wave,
It may be a step wave, a triangular wave, a sawtooth wave, etc.

〔作用〕[Effect]

本発明の方法により異常析出が効果的に防止さ
れる理由は必ずしも明らかではないが、次のよう
に推測される。即ち、前述の諸因子による形成さ
れたデンドライト前駆体が異常析出へと成長する
過程には、カソードの近傍に形成される拡散二重
層が重要な役割を果し、カソード近傍のカチオン
が電着により消費されて拡散二重層の濃度勾配が
大きくなるためにデンドライト前駆体が突起状に
成長し、この突起に高電流密度の電流が流れて突
起が加速度的に成長し異常析出になる。本発明の
方法により通電を間欠的に停止すると停止時間中
にカソード表面の沖合から拡散二重層へカチオン
の移動が起つて拡散二重層の濃度勾配が緩和さ
れ、その結果デンドライト前駆体の成長が抑制さ
れるものと考えられる。
The reason why abnormal precipitation is effectively prevented by the method of the present invention is not necessarily clear, but it is presumed as follows. In other words, the diffusion double layer formed near the cathode plays an important role in the process in which the dendrite precursors formed due to the above-mentioned factors grow into abnormal precipitation, and the cations near the cathode are absorbed by electrodeposition. As dendrite precursors are consumed and the concentration gradient of the diffusion double layer increases, the dendrite precursors grow into protrusions, and a current with a high current density flows through these protrusions, causing the protrusions to grow at an accelerated pace and become abnormally precipitated. When the current supply is stopped intermittently according to the method of the present invention, cations move from offshore of the cathode surface to the diffused double layer during the stopped time, and the concentration gradient of the diffused double layer is relaxed, and as a result, the growth of dendrite precursors is suppressed. It is considered that the

以下に本発明の実施例を比較例と共に示す。 Examples of the present invention are shown below along with comparative examples.

〔実施例〕〔Example〕

実施例…メツキ浴としてSnSO4を30g/、
H2SO4を120g/、スタータークルモ(レイ
ボルト(株)の錫メツキ用添加剤の商品名)を40
ml/含有せしめたものを用い、カソードロツ
カーを備えたメツキ装置で錫をアノードとし、
カソードラツクに取付けた42アロイのテストピ
ースに錫メツキを行つた。メツキ条件は極間距
離200mm、陰極電流密度1.5A/dm2、温度20℃
とし、通電と通電停止の時間をそれぞれ60秒、
5秒とした。この条件で9分間メツキしたが、
異常析出は認められなかつた。
Example...30g/SnSO 4 as a plating bath,
120g of H 2 SO 4 , 40g of Starter Kurumo (trade name of tin plating additive made by Raybolt Co., Ltd.)
ml/ml, using a plating device equipped with a cathode locker, using tin as an anode,
A 42 alloy test piece attached to a cathode rack was tin-plated. The plating conditions are: distance between electrodes 200mm, cathode current density 1.5A/dm 2 , temperature 20℃
The energization and de-energization times are each 60 seconds,
It was set to 5 seconds. I plucked for 9 minutes under these conditions,
No abnormal precipitation was observed.

比較例…実施例と同じメツキ浴、装置を用い、通
常の直流メツキとした外は実施例と同じメツキ
条件に従つて8分間メツキを行なつた。テスト
ピース上に長さ約100μの針状析出が認められ
た。
Comparative Example: Plating was carried out for 8 minutes using the same plating bath and equipment as in the example, and under the same plating conditions as in the example, except that normal direct current plating was used. Acicular deposits approximately 100μ in length were observed on the test piece.

〔発明の効果〕〔Effect of the invention〕

本発明により電気錫メツキにおける針状、糸状
の異常析出が効果的に防止され、メツキ物の信頼
性向上、製品歩留向上に大きく寄与できた。本発
明の方法は被メツキ物の前処理や下地メツキが不
要であり、又特別の添加剤を使用しないのでその
管理なども不要であり、簡便、低廉でかつ安定し
た実用性の高い方法である。
The present invention has effectively prevented needle-like and thread-like abnormal precipitation during electroplating, and has greatly contributed to improving the reliability of plated products and improving product yield. The method of the present invention does not require pretreatment of the object to be plated or base plating, and since no special additives are used, there is no need to manage them, making it a simple, inexpensive, stable, and highly practical method. .

Claims (1)

【特許請求の範囲】[Claims] 1 硫酸塩浴、硼弗化物浴等のメツキ浴を用いる
電気錫メツキ法において、通電を間欠的に停止す
ることを特徴とする電気錫メツキ法。
1. An electric tinning method using a plating bath such as a sulfate bath or a borofluoride bath, which is characterized by intermittent stopping of current supply.
JP26608685A 1985-11-28 1985-11-28 Electric tinning method Granted JPS62127493A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP26608685A JPS62127493A (en) 1985-11-28 1985-11-28 Electric tinning method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP26608685A JPS62127493A (en) 1985-11-28 1985-11-28 Electric tinning method

Publications (2)

Publication Number Publication Date
JPS62127493A JPS62127493A (en) 1987-06-09
JPH0573837B2 true JPH0573837B2 (en) 1993-10-15

Family

ID=17426141

Family Applications (1)

Application Number Title Priority Date Filing Date
JP26608685A Granted JPS62127493A (en) 1985-11-28 1985-11-28 Electric tinning method

Country Status (1)

Country Link
JP (1) JPS62127493A (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2614521B2 (en) * 1990-01-18 1997-05-28 株式会社小松製作所 Engine fuel injection pump
JPH04112821U (en) * 1991-03-14 1992-10-01 合同製鐵株式会社 Belt tension adjustment device for belt conveyor equipment
JPH0798997B2 (en) * 1992-09-04 1995-10-25 株式会社イケックス工業 Metal electrodeposition method
DE602005022650D1 (en) 2004-04-26 2010-09-16 Rohm & Haas Elect Mat Improved plating process

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5814520A (en) * 1981-07-17 1983-01-27 松下電器産業株式会社 Method of producing aluminum electrolytic condenser

Also Published As

Publication number Publication date
JPS62127493A (en) 1987-06-09

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