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Designated Contracting States: |
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DE FR GB IT NL |
| (30) |
Priority: |
04.07.1986 JP 156361/86
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| (43) |
Date of publication of application: |
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10.02.1988 Bulletin 1988/06 |
| (73) |
Proprietors: |
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- Daiwa Fine Chemicals Co., Ltd.
Kobe-shi
Hyogo-ken (JP)
- Ishihara Chemical Co., Ltd.
Kobe-shi
Hyogo-ken (JP)
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| (72) |
Inventors: |
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- Masaki, Seishi
Nagatu-ku
Kobe-shi
Hyogo-ken (JP)
- Tsuji, Kiyotaka
Kobe-shi
Hyogo-ken (JP)
- Okuhama, Yoshiaki
Higashinada-ku
Kobe-shi
Hyogo-ken (JP)
- Akutsu, Toshiji
Miki-shi
Hyogo-ken (JP)
|
| (74) |
Representative: Schwan, Gerhard, Dipl.-Ing. |
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Elfenstrasse 32 81739 München 81739 München (DE) |
| (56) |
References cited: :
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- CHEMICAL ABSTRACTS, vol. 76, no. 14, 3rd April 1972, page 573, 80287f, Columbus, Ohio,
US; SU-A-322 414 (KHARKOV CONSTRUCTION-ENGINEERING INSTITUTE) 30-11-1971
- GALVANOTECHNIK, vol. 66, no. 7, 1975, page 50; S. SRIVEERARAGHAVAN: "Galvanische Abscheidung
von Wismut"
- METAL FINISHING, vol. 61, no. 5, May 1963, pages 58,59; J.A. McCARTHY: "Bismuth plating
on steel from alkaline electrolytes"
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Remarks: |
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The file contains technical information submitted after the application was filed
and not included in this specification |
|
BACKGROUND OF THE INVENTION
[0001] This invention relates to bismuth and bismuth alloy plating baths. More particularly,
it is concerned with bismuth and bismuth alloy electroplating baths which use an organic
sulfonic acid as a co-soluble complex salt of bismuth and the metal other than bismuth
and give smooth electroplated deposits without the emission of highly polluting matter.
[0002] Bismuth is extensively used as a lubricant in nuclear reactor construction as well
as in such newly opened fields as the manufacture of rectifier and ohmic contacts.
These applications require relatively thick plates, approximately from 30 to 100 µm
in thickness. With conventional complex salt baths such as perchlorate, glycerate-tartrate,
and Trilon baths, however, the resulting deposits free of trees dendrite are at best
10 µm thick. Ordinary baths using no complex salt provide only coarse-crystal films.
[0003] Fast progress of the electronic industry in recent years has created demands for
various bismuth-base alloys of low-melting points. Increasing importance is being
attached to these low-melting solders because of the introduction of semiconductors
with more and more delicate thermal properties. Ordinary solders, typified by the
Sn-Pb alloy, have the disadvantage of so-called low-temperature brittleness. Component
parts soldered with them become brittle when placed in environments below ordinary
temperature, as are encountered by the soldered parts of devices and apparatus for
use in superconductive and space development projects. For services in such severe
environments, therefore, low-temperature resistant solders are desirable. Examples
are Bi-Sn, Bi-In, Bi-Pb, Bi-Co, Bi-Ni, Bi-Sb, Bi-In-Sn. and Bi-Sn-Pb alloys. Since
the standard electrode potential of bismuth is far nobler than those of tin, indium,
and lead, there occurs practically no codeposition of these alloying elements from
their simple solution. To make their deposition potentials as close to one another
as possible, a complex salt bath must be used instead.
[0004] Varied Bi-Sn alloy plating baths, for example, in the form of sulfate, chloride,
perchlorate, borofluoride, and alkali baths, have hitherto been reported. Nevertheless,
because of the electric potential difference, it is difficult to codeposit a relatively
large proportion of bismuth to tin, and an electrodeposit of the low-melting alloy
can hardly be obtained. As for the Bi-In alloy plating from a perchlorate bath, the
limitation to the current density range over which the codeposit is formed makes it
rarely possible to obtain thick, good alloy plates.
SUMMARY OF THE INVENTION
[0005] The present invention has resulted from investigations made in view of the foregoing.
It is aimed at providing a plating bath which consists essentially of an organic sulfonic
acid that seldom poses a pollution problem and salts of bismuth and a metal other
than bismuth, and gives substantially better electrodeposits than those from conventional
inorganic acid baths, and permits easy control of the bath in alloy plating, inasmuch
as the electrodeposit composition is close to the metal proportion in the bath. Thus
the investigations have led to the discovery of useful acids for the above purpose.
[0006] In the case of Bi-Sn alloy plating, a major disadvantage is that, where the electric
potential difference between tin and bismuth is too wide for the passage of current,
bismuth can be lost by its contact deposition on the anode tin surface. It has now
been found that the plating bath of the invention characteristically inhibits to a
large measure the unwanted bismuth deposition on the anode tin surface.
DETAILED DESCRIPTION OF THE INVENTION
[0007] The organic sulfonic acids to be used in accordance with the invention are sulfonic
acids as aliphatic or nonbenzene alicyclic compounds of the general formula
(X₁)
n-R-SO₃H
wherein R is a C₁₋₅ alkyl radical, X₁ is a halogen atom or hydroxyl, aryl, alkylaryl,
carboxyl, or sulfonyl radical which may be in any optional position of the alkyl radical,
and n is an integer of 0 to 3.
[0008] Examples of these organic sulfonic acids are methanesulfonic, ethanesulfonic, propanesulfonic,
2-propanesulfonic, butanesulfonic, 2-butanesulfonic, pentanesulfonic, chloropropanesulfonic,
2-hydroxyethane-1-sulfonic, 2-hydroxypropane-1-sulfonic, 2-hydroxybutane-1-sulfonic,
2-hydroxypentanesulfonic, allylsulfonic, 2-sulfoacetic, 2- or 3-sulfopropionic, sulfosuccinic,
sulfomaleic, sulfofumaric acids. These acids are used alone or as a mixture of two
or more. Their bismuth salts and salts of metals other than bismuth are prepared in
the usual manner.
[0009] A bismuth plating bath contains such an organic sulfonic acid and its bismuth salt.
In the case of a bismuth alloy plating bath, such an organic sulfonic acid, its bismuth
salt, and another or two or more metal salts are contained.
[0010] The total concentration of bismuth and another metal or metals is, in terms of the
metals, from 0.5 to 200 g/ℓ, preferably from 10 to 100 g/ℓ. The concentration of the
free organic sulfonic acid to be present in the plating bath is stoichiometrically
at least an equivalent to the bismuth or other metal ions in the bath. Preferably,
the concentration of the free organic sulfonic acid is 30-400 g/ℓ.
[0011] The plating bath of the invention may contain peptone, gelatin, nonionic surfactant,
or other additive effective in avoiding burnt deposits due to excessive current intensity
and in inhibiting dendritic growth. The concentration of the additive usually ranges
from 0.01 to 50 g/ℓ, preferably from 0.05 to 20 g/ℓ. Among typical nonionic surfactants
for this use are "Evan 740", "Liponox N-105", and "Neugen EN" (all trade names).
EXAMPLES
[0012] While the present invention is illustrated by the following several examples in which
certain plating bath compositions and operating conditions are used, it should be
noted that the invention is not limited thereto but may be variously embodied with
changes in the compositions and conditions to realize the objects of obtaining uniform,
smooth plated deposits.
[0013] Throughout the examples, the outward appearance of the plate obtained was evaluated
by the Hull cell test.
Example 1
[0014]

Example 2
[0015]

Example 3
[0016]

[0017] With the plating baths of Examples 1 to 3, Hull cell tests were conducted under the
conditions of 1 A and 5 min. Each example gave a grayish white smooth electrodeposit.
Example 4
[0018]

Example 5
[0019]

[0020] The plating baths of Examples 4 and 5 were subjected to Hull cell tests under the
conditions of 1 A and 5 min. All gave grayish white smooth electrodeposits.
[0021] In order to confirm the composition of the electrodeposit formed by the bismuth alloy
plating, plating was carried out by 600-coulomb constant current electrolysis, using
a stainless steel plate (0.3 x 3 x 5 cm) as the cathode, with cathode rocking at a
rate of 2 m/min, while varying the current density over a range of 0.5 - 3 A/dm².
After each run the electrodeposit formed was scraped off by a knife and dissolved
in 6N-HNO₃ with the application of heat. Tin was separated and the bismuth in the
solution was determined by the atomic absorption-spectroscopy.
The results are given in Table 1.
Table 1
| Dk (A/dm²) |
0.5 |
1.0 |
2.0 |
3.0 |
| Bi in electrodeposit, % |
26.0 |
20.4 |
13.8 |
15.3 |
| Current efficiency, % |
89.2 |
90.3 |
73.2 |
56.4 |
1. A bismuth or bismuth alloy plating bath comprising as essential ingredients an organic
sulfonic acid of the general formula
(X₁)n-R-SO₃H
wherein R is a C₁₋₅ alkyl radical, X₁ is a halogen atom or hydroxyl, carboxyl, or
sulfonyl radical which may be in any optional position of the alkyl radical, and n
is an integer of 0 to 3, and a bismuth salt of the acid or a mature of the bismuth
salt of the acid and one or more other metal salts of the acid, said bismuth salt
or salts of bismuth and one or more other metal of the organic acid being used at
a concentration, in terms of the respective metallic elements, of 0.5 to 200 g per
liter of the bath, and the concentration of the free organic sulfonic acid in the
plating bath being 30 to 400 g per liter of the bath and being stoichiometrically
at least an equivalent to the bismuth or other metal ions in the bath.
1. Bain de métallisation contenant du bismuth ou un alliage de bismuth, comprenant comme
ingrédients essentiels un acide sulfonique organique de formule générale
(X₁)n-R-SO₃H
dans laquelle R est un radical alkyle en c₁ à c₅, X₁ est un atome d'halogène ou un
radical hydroxyle, carboxyle ou sulfonyle qui peut occuper n'importe quelle position
sur le radical alkyle, et n est un nombre entier de 0 à 3, et un sel de bismuth de l'acide ou un mélange du sel
de bismuth de l'acide et d'un ou plusieurs autres sels métalliques de l'acide, ledit
sel de bismuth ou lesdits sels de bismuth et d'un ou plusieurs autres métaux de l'acide
organique étant utilisés à une concentration, en termes d'éléments métalliques respectifs,
de 0,5 à 200 g par litre du bain, et la concentration de l'acide sulfonique organique
libre dans le bain de métallisation étant de 30 à 400 g par litre du bain et étant
stoechiométriquement au moins l'équivalent du bismuth ou des autres ions métalliques
dans le bain.
1. Wismut- oder Wismutlegierungs-Plattierbad das als wesentliche Bestandteile eine organische
Sulfonsäure der allgemeinen Formel
(X₁)n-R-SO₃H,
wobei R ein C₁₋₅-Alkylradical, X₁ ein Halogenatom oder ein Hydroxyl-, Carboxyl- oder
Sulfonylradikal, das an jeder beliebigen Position des Alkylradikals stehen kann, und
n eine ganze Zahl von 0 bis 3 ist, und ein Wismutsalz der Säure oder ein Gemisch des
Wismutsalzes der Säure und eines oder mehrerer anderer Metallsalze der Säure enthält,
wobei das Wismutsalz oder Salze von Wismut und einem oder mehreren anderen Metall(en)
der organischen Säure in einer Konzentration von 0,5 bis 200 g pro Liter des Bades,
bezogen auf die betreffenden metallischen Elemente, verwendet sind und die Konzentration
der freien organischen Sulfonsäure in dem Plattierbad 30 bis 400 g pro Liter des Bades
beträgt und stöchiometrisch mindestens äquivalent zu den Wismut- oder anderen Metallionen
in dem Bad ist.