EP0241415B1 - Acid tin-(II)-containing electrolyte - Google Patents

Acid tin-(II)-containing electrolyte Download PDF

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Publication number
EP0241415B1
EP0241415B1 EP87810159A EP87810159A EP0241415B1 EP 0241415 B1 EP0241415 B1 EP 0241415B1 EP 87810159 A EP87810159 A EP 87810159A EP 87810159 A EP87810159 A EP 87810159A EP 0241415 B1 EP0241415 B1 EP 0241415B1
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Prior art keywords
diphenylamine
amino
sulphonic acid
electrolyte
acid
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German (de)
French (fr)
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EP0241415A1 (en
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Jean-François Paulet
Bruno Boetsch
Fritz Schneeberger
Günther Tscheulin
Hans Bohler
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Sandoz AG
3A Composites International AG
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Sandoz AG
Alusuisse Lonza Services Ltd
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    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D3/00Electroplating: Baths therefor
    • C25D3/02Electroplating: Baths therefor from solutions
    • C25D3/30Electroplating: Baths therefor from solutions of tin
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D11/00Electrolytic coating by surface reaction, i.e. forming conversion layers
    • C25D11/02Anodisation
    • C25D11/04Anodisation of aluminium or alloys based thereon
    • C25D11/18After-treatment, e.g. pore-sealing
    • C25D11/20Electrolytic after-treatment
    • C25D11/22Electrolytic after-treatment for colouring layers
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D3/00Electroplating: Baths therefor
    • C25D3/02Electroplating: Baths therefor from solutions
    • C25D3/30Electroplating: Baths therefor from solutions of tin
    • C25D3/32Electroplating: Baths therefor from solutions of tin characterised by the organic bath constituents used

Definitions

  • Sn (II) salts are used in acidic solutions, e.g. used in the form of sulfate, fluoroborate or chloride solutions.
  • Sn (II) is oxidized to Sn (IV) during the working process.
  • stabilizers By adding substances to the electrolyte, so-called stabilizers, the oxidation can be more or less prevented, i.e. Sn (II) can be more or less stabilized.
  • the effectiveness of the stabilizer is decisive for the quality of the precipitation or the coloring of the anodized layer. It is generally known that, in the presence of both types of ions Sn (II) and Sn (IV), the quality of the surface treatment deteriorates in considerable amounts due to insufficient stabilization of the Sn (II). It is therefore desirable to obtain the tin in acidic solutions as Sn (II).
  • organic aromatic compounds are also known as stabilizers which contain amino groups, e.g. Aminophenol, dimethylaniline.
  • the invention is therefore based on the object of providing a process for coloring anodized aluminum or aluminum alloys using an acidic electrolyte containing Sn (II), which contains substances with a well-stabilizing effect of Sn (II) ions and a better scattering and thus coupled has a better current distribution.
  • an electrolyte which, by adding a compound of the formula I which is soluble in an acid medium, wherein R1 to R10 independently of one another are hydrogen, halogen (at most once in each ring), nitro (at most once in each ring), -COOM (at most two in each ring), -SO3M (at most two in each ring), C1 ⁇ 4alkyl, -NH2 (at most two in each ring) or phenylamino (at most once in each ring), R11 represents hydrogen, C1 ⁇ 4alkyl, hydroxy-C1 ⁇ 4alkyl, phenyl or a group - (BO) n -R12 (a), where each B, independently of one another, is -C2H4-, -C3H6- or -C4H8-, n is a number from 1 to 20, and R12 is hydrogen, -SO3M or -CH2COOM, and M is hydrogen or a cation
  • the groups R1 to R10 are preferably H, -NH2, -COOM or -SO3M and R11 is preferably hydrogen or a group (a), in which n is a number from 1-5.
  • Diphenylamine-4-sulfonic acid or a mixture of this compound with diphenylamine-4,4'-disulfonic acid is preferably used.
  • test series 1 The same stock solution was prepared as in test series 1, which was placed in the same vessels of 1 liter of electrolyte as in test series 1. In all baths the pH was 1; the baths were at room temperature and were constantly moved with a magnetic stirrer.
  • Bath 10 thus corresponds to bath 5 of test series 1.
  • test series 1 and 2 which contain the additives to be used according to the invention
  • dyeing tests with anodically oxidized aluminum layers were carried out in 60 liter baths.
  • the voltage was 15 volts in all cases, the treatment time varied between 1 and 12 minutes.
  • the sample plates consisted of PERALUMAN-100 (semi-hard), an aluminum alloy with 1% magnesium, and had the dimensions 200 x 300 x 1.5 mm.
  • the plates were anodized according to normal direct current / H2SO4 method.
  • the layer thickness was 20 »m.
  • Amounts of 1 g of the additives used according to the invention per liter of electrolyte were found as a sensible upper limit, without wishing to be determined, and accordingly about 20 mg as a sensible lower limit. A mixture or combination of different additives does not interfere. Additional amounts beyond this have practically no additional effect. Quantities of 20 to 500 mg / l, preferably 10 to 20 mg / l, of electrolyte have proven to be advantageous.

Abstract

In acid Sn(II)-containing electrolytes for staining anodically produced oxide layers on aluminium or aluminium alloys or for electroplating, the Sn(II) becomes oxidised. Adding substances to the electrolyte, so called stabilisers, may prevent the oxidation to a greater or lesser degree, i.e. Sn(II) can be stabilised to a greater or lesser degree. The effectiveness of the stabiliser furthermore governs the quality of the deposits or the coloration of the anodised layer. The quality of the surface treatment is known to deteriorate in the presence of Sn(IV) in substantial amounts alongside Sn(II) as a consequence of inadequate stabilisation of the Sn(II). An acid Sn(II)-containing electrolyte with a soluble diphenylamine or substituted diphenylamine derivative added stabilises the Sn(II) and yields faultless colorations.

Description

Die Erfindung betrifft ein Verfahren zum Färben von anodisch erzeugten Oxidschichten auf Aluminium oder Aluminiumlegierungen mit einem sauren Sn(II)-haltigen Elektrolyten, der durch bestimmte Zusätze stabilisiert ist, die dafür verwendete Sn(II)-Elektrolytzusammensetzung an sich und deren Verwendung für das Färben von anodisiertem Aluminium oder Aluminiumlegierungen.The invention relates to a method for dyeing anodically produced oxide layers on aluminum or aluminum alloys with an acidic Sn (II) -containing electrolyte, which is stabilized by certain additives, the Sn (II) electrolyte composition used therefor and its use for the dyeing of anodized aluminum or aluminum alloys.

Sowohl beim Galvanisieren als auch beim Färben von anodisch aufgebrachten Aluminiumoxidschichten auf Aluminium oder Aluminiumlegierungen werden in sauren Lösungen Sn(II)-Salze z.B. in Form von Sulfat-, Fluoroborat- oder Chloridlösungen verwendet.Both in electroplating and in the dyeing of anodically applied aluminum oxide layers on aluminum or aluminum alloys, Sn (II) salts are used in acidic solutions, e.g. used in the form of sulfate, fluoroborate or chloride solutions.

Es ist bekannt, dass praktisch nur das saure Sulfatbad einfache Sn(II)-Ionen enthält. Bei allen anderen Elektrolyten ist das Zinn mindestens teilweise komplex gebunden.It is known that practically only the acidic sulfate bath contains simple Sn (II) ions. With all other electrolytes, the tin is at least partially complexly bound.

Eine Schwierigkeit beim Galvanisieren bzw. beim Einfärben von anodisch erzeugten Oxidschichten auf Aluminium oder Aluminiumlegierungen in sauren Lösungen besteht darin, dass das Sn(II) während des Arbeitsprozesses zu Sn(IV) aufoxidiert wird. Durch Zugabe von Substanzen zum Elektrolyten, sogenannten Stabilisatoren, kann die Oxidation mehr oder weniger verhindert werden, d.h. Sn(II) kann mehr oder weniger stabilisiert werden.A difficulty in electroplating or coloring anodically produced oxide layers on aluminum or aluminum alloys in acidic solutions is that the Sn (II) is oxidized to Sn (IV) during the working process. By adding substances to the electrolyte, so-called stabilizers, the oxidation can be more or less prevented, i.e. Sn (II) can be more or less stabilized.

Die Wirksamkeit des Stabilisators ist ausschlaggebend für die Güte der Niederschläge bzw. der Einfärbung der Eloxalschicht. Es ist allgemein bekannt, dass sich bei Anwesenheit beider Ionenarten Sn(II) und Sn(IV) durch unzureichende Stabilisierung des Sn(II) in erheblichen Mengen die Güte der Oberflächenbehandlung verschlechtert. Es ist also danach zu trachten, das Zinn in sauren Lösungen als Sn(II) zu erhalten.The effectiveness of the stabilizer is decisive for the quality of the precipitation or the coloring of the anodized layer. It is generally known that, in the presence of both types of ions Sn (II) and Sn (IV), the quality of the surface treatment deteriorates in considerable amounts due to insufficient stabilization of the Sn (II). It is therefore desirable to obtain the tin in acidic solutions as Sn (II).

Aus FR-A 2095375 (1) und GB-A 1089479 (2) sind Verfahren zum Galvanisieren von Zinn bekannt, deren Verbesserung darin besteht, dass durch bestimmte Zusätze zum Galvanisierbad eine erwünschte Ausdehnung des Bereiches der anwendbaren Stromdichten erreicht wird.
In (1) erfüllt diesen Zweck ein Zwei-Komponenten-Zusatz, wobei als 1. Komponente u.a. eine aromatische Verbindung mit basischem Stickstoffatom wie beispielsweise Diphenylamin, N,N-Diphenylmethylamin und 2,4-Diaminodiphenylamin genannt sind.
In (2) gehört dieser Zusatz beispielsweise der Klasse der aromatischen Amine wie Aminodiphenylmethan und Derivaten davon an.
From FR-A 2095375 (1) and GB-A 1089479 (2) methods for electroplating tin are known, the improvement of which consists in that a desired extension of the range of the applicable current densities is achieved by certain additives to the electroplating bath.
In (1) a two-component addition fulfills this purpose, an aromatic compound with a basic nitrogen atom such as diphenylamine, N, N-diphenylmethylamine and 2,4-diaminodiphenylamine being mentioned as the first component.
In (2) this addition belongs, for example, to the class of aromatic amines such as aminodiphenylmethane and derivatives thereof.

Bei sauren Elektrolyten sind auch organische aromatische Verbindungen als Stabilisatoren bekannt, die Aminogruppen enthalten z.B. Aminophenol, Dimethylanilin.In the case of acidic electrolytes, organic aromatic compounds are also known as stabilizers which contain amino groups, e.g. Aminophenol, dimethylaniline.

Diese Verbindungen haben einen stabilisierenden Effekt für Sn(II). Sie können es jedoch nicht verhindern, dass ein Teil des Sn(II) zu Sn(IV) oxidiert wird. Dadurch wird besonders die Qualität der Färbung von anodisch erzeugten Oxidschichten auf Aluminium oder Aluminiumlegierungen beeinflusst. Bei unzureichender Stabilisierung von Sn(II) ist die Farbtiefe von dunklen Farbtönen und die Gleichmässigkeit der Färbung oft mangelhaft. Hierin liegt ein wesentlicher Nachteil der bisher verwendeten Stabilisatoren. Ein idealer Stabilisator wäre einer, der die vollständige Stabilisation des Sn(II)-Ions bewirkt. Tatsächlich ist es aber schwierig, beim Färben von anodisch erzeugten Oxidschichten auf Aluminium oder Aluminiumlegierungen Farben wie Dunkelbronze oder Schwarz bei Verwendung der oben angeführten Zusätze herzustellen. Meist lässt zusätzlich die Streuung des Elektrolyten zu wünschen übrig. Dies macht sich durch hellere und dunklere Färbung der Randzonen bemerkbar. Mit fortgeschrittener Färbezeit der Eloxalschicht - ab etwa 10 Minuten - treten Ueberfärbungen auf und man erhält einen metallischen Belag auf der Oberfläche, was Reinigungsprobleme der gefärbten Oberfläche, Verunreinigungen der Verdichtungsbäder und Korrosionsprobleme nach sich zieht.These compounds have a stabilizing effect for Sn (II). However, you cannot prevent part of the Sn (II) from being oxidized to Sn (IV). This particularly affects the quality of the coloring of anodic oxide layers on aluminum or aluminum alloys. If Sn (II) is not sufficiently stabilized, the depth of color of dark shades and the uniformity of the coloration are often poor. This is a major disadvantage of the stabilizers previously used. An ideal stabilizer would be one that effects full stabilization of the Sn (II) ion. In fact, when coloring anodized oxide layers on aluminum or aluminum alloys, it is difficult to produce colors such as dark bronze or black using the additives mentioned above. Usually the scattering of the electrolyte also leaves something to be desired. This is noticeable by the lighter and darker coloring of the edge zones. With an advanced coloring time of the anodized layer - from about 10 minutes - over-coloring occurs and a metallic coating is obtained on the surface, which results in cleaning problems of the colored surface, contamination of the compression baths and corrosion problems.

Der Erfindung liegt somit die Aufgabe zugrunde, ein Verfahren zum Färben von anodisiertem Aluminium oder Aluminiumlegierungen bereitzustellen unter Verwendung eines sauren Sn(II)-haltigen Elektrolyten, der Substanzen mit gut stabilisierendem Effekt von Sn(II)-Ionen enthält und eine bessere Streuung und damit gekoppelt eine bessere Stromverteilung hat.The invention is therefore based on the object of providing a process for coloring anodized aluminum or aluminum alloys using an acidic electrolyte containing Sn (II), which contains substances with a well-stabilizing effect of Sn (II) ions and a better scattering and thus coupled has a better current distribution.

Erfindungsgemäss wird die gestellte Aufgabe durch einen Elektrolyten gelöst, welcher durch Zusatz einer in saurem Medium löslichen Verbindung der Formel I,

Figure imgb0001

worin R₁ bis R₁₀ unabhängig voneinander Wasserstoff, Halogen (höchstens einmal in jedem Ring), Nitro (höchstens einmal in jedem Ring), -COOM (höchstens zwei in jedem Ring), -SO₃M (höchstens zwei in jedem Ring), C₁₋₄Alkyl, -NH₂ (höchstens zwei in jedem Ring) oder Phenylamino (höchstens einmal in jedem Ring) bedeuten, R₁₁ für Wasserstoff, C₁₋₄Alkyl, Hydroxy-C₁₋₄alkyl, Phenyl oder eine Gruppe -(B-O)n-R₁₂ (a) steht, wobei jedes B, unabhängig voneinander, für -C₂H₄-, -C₃H₆- oder -C₄H₈-, n für eine Zahl von 1 bis 20, und R₁₂ für Wasserstoff, -SO₃M oder -CH₂COOM stehen, und M Wasserstoff oder ein Kation bedeutet, oder einer Mischung solcher Verbindungen der Formel I stabilisiert ist.According to the invention, the object is achieved by an electrolyte which, by adding a compound of the formula I which is soluble in an acid medium,
Figure imgb0001

wherein R₁ to R₁₀ independently of one another are hydrogen, halogen (at most once in each ring), nitro (at most once in each ring), -COOM (at most two in each ring), -SO₃M (at most two in each ring), C₁₋₄alkyl, -NH₂ (at most two in each ring) or phenylamino (at most once in each ring), R₁₁ represents hydrogen, C₁₋₄alkyl, hydroxy-C₁₋₄alkyl, phenyl or a group - (BO) n -R₁₂ (a), where each B, independently of one another, is -C₂H₄-, -C₃H₆- or -C₄H₈-, n is a number from 1 to 20, and R₁₂ is hydrogen, -SO₃M or -CH₂COOM, and M is hydrogen or a cation, or a mixture of such compounds of formula I is stabilized.

Beim Einsatz von Verbindungen der Formel I in Elektrolysebädern treten überraschenderweise während des Färbeprozesses von anodisch oxidierten Aluminiumschichten Fehler bezüglich Ueberfärbung bei fortgeschrittener Färbezeit nicht mehr auf. Der Mangel, dass oft dunkle Farbtöne nur unzureichend erhalten wurden, und die Ungleichmässigkeit der Färbung, die beim Färben der Schichten in Anwesenheit der bisher üblichen Stabilisatoren immer wieder auftraten, sind durch die erfindungsgemässen Zusätze wesentlich verbessert oder ganz verhindert worden. Die ausgezeichneten Färbeeigenschaften betreffen nicht nur die hellen Farbtöne, sondern ganz besonders auch die dunklen, die gerade bis anhin sehr schwer sowohl bezüglich Farbtiefe als auch Gleichmässigkeit der Färbung zu erreichen waren.When compounds of the formula I are used in electrolysis baths, surprisingly, errors relating to over-coloration no longer occur during the dyeing process of anodically oxidized aluminum layers with advanced dyeing time. The lack that dark shades were often inadequately obtained and the unevenness of coloration that repeatedly occurred when the layers were colored in the presence of the stabilizers customary hitherto have been substantially improved or completely prevented by the additives according to the invention. The excellent coloring properties apply not only to the light shades, but entirely especially the dark ones, which until now were very difficult to achieve both in terms of depth of color and uniformity of color.

Von besonderer Ueberraschung ist es, dass diese Verbindungen bereits in sehr kleinen Konzentrationen hochwirksam sind. So bewirkt schon ein Zusatz von 20 ppm einen erheblichen Stabilisierungseffekt.It is particularly surprising that these compounds are highly effective even in very small concentrations. Even an addition of 20 ppm has a significant stabilizing effect.

Gesamthaft wurde somit festgestellt, dass die eingangs erwähnten Nachteile bekannter Stabilisatoren für saure Sn(II)-haltige Elektrolyten zum Färben von anodisch oxidierten Aluminiumschichten in den erfindungsgemäss verwendeten Elektrolyten nicht oder nur in nicht störendem und damit vernachlässigbarem Masse auftraten.Overall, it was found that the disadvantages mentioned at the outset of known stabilizers for acidic Sn (II) -containing electrolytes for coloring anodized aluminum layers did not occur in the electrolytes used according to the invention, or only to a non-disturbing and therefore negligible extent.

In Verbindungen der Formel I sind die Gruppen R₁ bis R₁₀ bevorzugt H, -NH₂, -COOM oder -SO₃M und ist R₁₁ bevorzugt Wasserstoff oder eine Gruppe (a), worin n eine Zahl von 1-5 bedeutet.In compounds of formula I, the groups R₁ to R₁₀ are preferably H, -NH₂, -COOM or -SO₃M and R₁₁ is preferably hydrogen or a group (a), in which n is a number from 1-5.

Aus der beschriebenen Verbindungsgruppe der Formel I sind die folgenden Substanzen und deren Mischungen als Zusatz besonders vorteilhaft:
   2-Amino-diphenylamin
   4-Amino-diphenylamin
   4-Amino-diphenylamin-2-carbonsäure
   Diphenylamin-4-sulfonsäure
   2-Amino-diphenylamin-4-sulfonsäure
   4-Amino-diphenylamin-2-sulfonsäure
   4,4'-Diamino-diphenylamin-2-sulfonsäure
   4'-Amino-4-nitrodiphenylamin-2-sulfonsäure
   1-Amino-2,4-di(phenylamino)benzol-5-sulfonsäure und
   Diphenylamin-4,4'-disulfonsäure.
The following substances and their mixtures from the described group of compounds of formula I are particularly advantageous as additives:
2-amino-diphenylamine
4-amino-diphenylamine
4-amino-diphenylamine-2-carboxylic acid
Diphenylamine-4-sulfonic acid
2-amino-diphenylamine-4-sulfonic acid
4-amino-diphenylamine-2-sulfonic acid
4,4'-diamino-diphenylamine-2-sulfonic acid
4'-amino-4-nitrodiphenylamine-2-sulfonic acid
1-amino-2,4-di (phenylamino) benzene-5-sulfonic acid and
Diphenylamine-4,4'-disulfonic acid.

Vorzugsweise wird Diphenylamin-4-sulfonsäure oder ein Gemisch dieser Verbindung mit Diphenylamin-4,4'-disulfonsäure eingesetzt.Diphenylamine-4-sulfonic acid or a mixture of this compound with diphenylamine-4,4'-disulfonic acid is preferably used.

Damit die Vorteile des erfindungsgemäss verwendeten Elektrolyten gegenüber den bisher benutzten vollkommen erkannt werden, müssen alle Faktoren - Stabilisierungswirkung des Sn(II), Streuung / Stromverteilung, Färbewirkung - selbstverständlich gemeinsam beurteilt werden.In order that the advantages of the electrolyte used according to the invention compared to those previously used are fully recognized, all factors - stabilizing effect of Sn (II), scattering / current distribution, coloring effect - must of course be assessed together.

Um hier den hervorragenden Effekt der Stabilisierung und die damit verbundenen besseren Färbeeigenschaften von anodisch erzeugten Oxidschichten auf Aluminium oder Aluminiumlegierungen in sauren Lösungen zu zeigen, werden die folgenden zwei Versuchsreihen und Färbeversuche angeführt. Zweck dieser Vergleichsversuche ist es, mit einem Schnelltest unter Begasung mit reinem Sauerstoff die stabilisierende Wirkung der jeweils verwendeten Zusätze zu zeigen.In order to show the excellent effect of stabilization and the associated better coloring properties of anodically produced oxide layers on aluminum or aluminum alloys in acidic solutions, the following two test series and coloring tests are given. The purpose of these comparative experiments is to show the stabilizing effect of the additives used in each case using a rapid test with gassing with pure oxygen.

Versuchsreihe 1Test series 1

Es wurde ein wässriger Elektrolyt hergestellt, bestehend aus H₂SO₄ (10 g/l) und SnSO₄ (20 g/l). Unter diesen Bedingungen liegt Zinn anfangs als Sn(II) vor. Der Elektrolyt wurde auf 7 Gefässe von gleicher geometrischer Form verteilt. In jedem Gefäss befand sich 1 Liter Elektrolyt.

Bad 1:
ohne Zusatz
Die anderen Bäder enthielten folgende Zusätze:
Bad 2:
Paraphenolsulfonsäure, 20 g/l, bisher üblicherweise verwendeter Zusatz
Bad 3:
N,N-Dimethylanilin, 100 mg/l, bekannter Zusatz
Bad 4:
Diphenylamin, 100 mg/l
Bad 5:
Diphenylamin-4-sulfonsäure, 100 mg/l
Bad 6:
2-Amino-diphenylamin-4-sulfonsäure, 100 mg/l
Bad 7:
4-Amino-diphenylamin-2-carbonsäure, 100 mg/l
In allen Bädern war der pH-Wert gleich 1; die Bäder befanden sich auf Raumtemperatur und wurden mit einem Magnetrührer ständig bewegt. Jedes Bad wurde durch eine Glasfritte mit 200 cm³ reinem Sauerstoff pro Minute begast und alle halbe Stunde wurde der Gehalt an Sn(II) analysiert. Die Ergebnisse sind in Figur 1 wiedergegeben (Ordinate: Verlust an Sn(II) in g/l; Abszisse: Zeit in Stunden).An aqueous electrolyte was prepared, consisting of H₂SO₄ (10 g / l) and SnSO₄ (20 g / l). Under these conditions, tin is initially available as Sn (II). The electrolyte was distributed over 7 vessels of the same geometric shape. There was 1 liter of electrolyte in each vessel.
Bathroom 1:
without addition
The other baths contained the following additives:
Bathroom 2:
Paraphenolsulfonic acid, 20 g / l, additive commonly used so far
Bathroom 3:
N, N-dimethylaniline, 100 mg / l, known additive
Bathroom 4:
Diphenylamine, 100 mg / l
Bathroom 5:
Diphenylamine-4-sulfonic acid, 100 mg / l
Bathroom 6:
2-amino-diphenylamine-4-sulfonic acid, 100 mg / l
Bathroom 7:
4-amino-diphenylamine-2-carboxylic acid, 100 mg / l
In all baths the pH was 1; the baths were at room temperature and were constantly moved with a magnetic stirrer. Each bath was gassed through a glass frit with 200 cc of pure oxygen per minute and the Sn (II) content was analyzed every half hour. The results are shown in FIG. 1 (ordinate: loss of Sn (II) in g / l; abscissa: time in hours).

Versuchsreihe 2Test series 2

Es wurde die gleiche Stammlösung wie in Versuchsreihe 1 hergestellt, die wie bei Versuchsreihe 1 in gleiche Gefässe zu je 1 Liter Elektrolyt gegeben wurde. In allen Bädern war der pH-Wert gleich 1; die Bäder befanden sich auf Raumtemperatur und wurden mit einem Magnetrührer ständig bewegt.The same stock solution was prepared as in test series 1, which was placed in the same vessels of 1 liter of electrolyte as in test series 1. In all baths the pH was 1; the baths were at room temperature and were constantly moved with a magnetic stirrer.

Das Bad 8 entsprach dem Bad 1 der Versuchsreihe 1 und enthielt keinen Zusatz. Die folgenden drei Bäder enthielten alle Diphenylamin-4-sulfonsäure und zwar in folgender Menge:

Bad 9:
20 mg/l
Bad 10:
100 mg/l
Bad 11:
200 mg/l .
Bath 8 corresponded to bath 1 of test series 1 and contained no additive. The following three baths all contained diphenylamine-4-sulfonic acid in the following amount:
Bathroom 9:
20 mg / l
Bathroom 10:
100 mg / l
Bathroom 11:
200 mg / l.

Bad 10 entspricht somit Bad 5 der Versuchsreihe 1.Bath 10 thus corresponds to bath 5 of test series 1.

Wie in Versuchsreihe 1 wurde jedes Bad mit 200 cm³ reinem Sauerstoff pro Minute durch eine Glasfritte begast und alle halbe Stunde der Sn(II)-Gehalt bestimmt. Die Ergebnisse sind in Figur 2 dargestellt (Ordinate: Verlust an Sn(II) in g/l: Abszisse: Zeit in Stunden).As in test series 1, each bath was gassed with 200 cm 3 of pure oxygen per minute through a glass frit and the Sn (II) content was determined every half hour. The results are shown in FIG. 2 (ordinate: loss of Sn (II) in g / l: abscissa: time in hours).

Aus den Figuren ist ersichtlich, dass ohne Zusatz schon nach relativ kurzer Zeit ein grosser Anteil des Sn(II) in Sn(IV) übergegangen ist. Ferner ist zu erkennen, dass der stabilisierende Effekt sowohl von der Zusatzsubstanz als auch von der Zusatzmenge abhängig ist. Obwohl von den bekannten Zusätzen Paraphenolsulfonsäure und N,N-Dimethylanilin viel grössere Mengen zugegeben wurden, ist deren Wirkung als Stabilisator für Sn(II) wesentlich schlechter als die der erfindungsgemäss verwendeten Zusätze.It can be seen from the figures that without addition, a large proportion of the Sn (II) has changed into Sn (IV) after a relatively short time. It can also be seen that the stabilizing effect is dependent both on the additional substance and on the additional amount. Although much larger amounts of the known additives paraphenolsulfonic acid and N, N-dimethylaniline have been added, their action as a stabilizer for Sn (II) is much worse than that of the additives used according to the invention.

FärbeversucheStaining attempts

Mit den in den Versuchsreihen 1 und 2 angegebenen Elektrolyten, welche die gemäss der Erfindung zu verwendenden Zusätze enthalten, wurden in 60 Liter-Bädern Färbeversuche mit anodisch oxidierten Aluminiumschichten durchgeführt. Die Spannung betrug in allen Fällen 15 Volt, die Behandlungszeit variierte zwischen 1 und 12 Minuten. Die Musterplatten bestanden aus PERALUMAN-100 (halbhart), einer Aluminiumlegierung mit 1% Magnesium, und hatten die Ausmasse 200 x 300 x 1,5 mm. Die Platten wurden gemäss normalem Gleichstrom/H₂SO₄-Verfahren anodisiert. Die Schichtdicke betrug 20 »m.With the electrolytes specified in test series 1 and 2, which contain the additives to be used according to the invention, dyeing tests with anodically oxidized aluminum layers were carried out in 60 liter baths. The voltage was 15 volts in all cases, the treatment time varied between 1 and 12 minutes. The sample plates consisted of PERALUMAN-100 (semi-hard), an aluminum alloy with 1% magnesium, and had the dimensions 200 x 300 x 1.5 mm. The plates were anodized according to normal direct current / H₂SO₄ method. The layer thickness was 20 »m.

In allen Fällen wurde eine vollkommene regelmässige Bronzefärbung erzielt, die frei von Randverfärbungen war. Bei den bisher gebräuchlichen Zusätzen treten gerade beim Bronzefarbton häufig Kanteneffekte auf, bedingt durch schlechte Streuung des Elektrolyten. Das bedeutet, dass bei dem erfindungsgemäss verwendeten Sn(II)-haltigen Elektrolyten die Streuung besser ist als bei den für diesen Zweck bisher gebräuchlichen Elektrolyten. Die Folge ist eine bessere Stromverteilung und damit verbunden eine regelmässigere Einfärbung der anodisch oxidierten Schicht.In all cases, a perfect regular bronze coloring was achieved, which was free from edge discoloration. With the additives that have been used up to now, edge effects often occur, particularly in the case of bronze color, due to poor scattering of the electrolyte. This means that with the Sn (II) -containing electrolyte used according to the invention, the scattering is better than with the electrolytes previously used for this purpose. The result is a better current distribution and associated with this a more regular coloring of the anodized layer.

Als sinnvolle obere Grenze, ohne sich dabei festlegen zu wollen, wurden Mengen von 1 g der erfindungsgemäss verwendeten Zusätze pro Liter Elektrolyt gefunden, dementsprechend als sinnvolle untere Grenze etwa 20 mg. Dabei stört eine Mischung oder Kombination von verschiedenen Zusätzen nicht. Darüber hinausgehende Zusatzmengen zeigen praktisch keine zusätzliche Wirkung mehr. Als vorteilhaft haben sich Mengen von 20 bis 500 mg/l, vorzugsweise 10 bis 20 mg/l Elektrolyt erwiesen.Amounts of 1 g of the additives used according to the invention per liter of electrolyte were found as a sensible upper limit, without wishing to be determined, and accordingly about 20 mg as a sensible lower limit. A mixture or combination of different additives does not interfere. Additional amounts beyond this have practically no additional effect. Quantities of 20 to 500 mg / l, preferably 10 to 20 mg / l, of electrolyte have proven to be advantageous.

Claims (9)

  1. Process for dyeing anodically produced oxide layers on aluminium or aluminum alloys, characterized in that an acidic Sn(II)-containing electrolyte is used, which is stabilized by adding a compound of formula I,
    Figure imgb0004
    which is soluble in an acidic medium, and
    wherein R₁ to R₁₀, independently of one another, signify hydrogen, halogen (at most one in each ring), nitro (at most one in each ring), -COOM (at most two in each ring), -SO₃M (at most two in each ring), C₁₋₄alkyl, -NH₂ (at most two in each ring) or phenylamino (at most one in each ring), R₁₁ is hydrogen, C₁₋₄alkyl, hydroxy-C₁₋₄alkyl, phenyl or a group -(B-O)n-R₁₂ (a), whereby each B, independently of one another, is -C₂H₄-, -C₃H₆-, -C₄H₈-, n is a number from 1 to 20, and R₁₂ is hydrogen, -SO₃M or -CH₂COOM, and M signifies hydrogen or a cation,
    or a mixture of such compounds of formula I.
  2. Process according to claim 1, characterized in that the electrolyte contains an admixture of diphenylamine-4-sulphonic acid or a mixture of this compound with diphenylamine-4,4'-disulphonic acid.
  3. Process according to claim 1 or 2, characterized in that the electrolyte contains the single or combined admixture in a quantity of 20 mg to 500 mg per litre of electrolyte.
  4. Use of a compound of formula I according to claim 1, or of a mixture thereof, for dyeing anodically produced oxide layers on aluminium or aluminium alloys, in an acidic Sn(II)-containing electrolyte.
  5. Use according to claim 4, whereby a compound from the series
       2-amino-diphenylamine
       4-amino-diphenylamine
       4-amino-diphenylamine-2-carboxylic acid
       diphenylamine-4-sulphonic acid
       2-amino-diphenylamine-4-sulphonic acid
       4-amino-diphenylamine-2-sulphonic acid
       4,4'-diamino-diphenylamine-2-sulphonic acid
       4'-amino-4-nitrodiphenylamine-2-sulphonic acid
       1-amino-2,4-di(phenylamino)benzene-5-sulphonic acid
       and diphenylamine-4,4'-disulphonic acid
    or a mixture thereof, is employed.
  6. Use according to claim 5, whereby diphenylamine-4-sulphonic acid is employed, or a mixture of this compound with diphenylamine-4,4'-disulphonic acid.
  7. Acidic Sn(II)-containing electrolyte for dyeing anodically produced oxide layers on aluminium or aluminium alloys, characterized in that the electrolyte contains a compound from the series
       4-amino-diphenylamine-2-carboxylic acid
       diphenylamine-4-sulphonic acid
       2-amino-diphenylamine-4-sulphonic acid
       4-amino-diphenylamine-2-sulphonic acid
       4,4'-diamino-diphenylamine-2-sulphonic acid
       4'-amino-4-nitrodiphenylamine-2-sulphonic acid
       1-amino-2,4-di(phenylamino)benzene-5-sulphonic acid
       and diphenylamine-4,4'-disulphonic acid
    or a mixture thereof.
  8. Acidic Sn(II)-containing electrolyte according to claim 7, characterized in that the electrolyte contains an admixture of diphenylamine-4-sulphonic acid, or a mixture of this compound with diphenylamine-4,4'-disulphonic acid.
  9. Acidic Sn(II)-containing electrolyte according to claim 7 or 8, characterized in that the electrolyte contains the single or combined admixture in a quantity of 20 mg to 500 mg per litre of electrolyte.
EP87810159A 1986-03-25 1987-03-19 Acid tin-(II)-containing electrolyte Expired - Lifetime EP0241415B1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CH1223/86 1986-03-25
CH122386 1986-03-25

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EP0241415B1 true EP0241415B1 (en) 1995-03-08

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JPH059765A (en) * 1991-07-04 1993-01-19 Nippon Parkerizing Co Ltd Acidic cleaning liquid for aluminum and cleaning method
JP7009679B2 (en) * 2015-07-29 2022-01-26 石原ケミカル株式会社 Electric tin and electric tin alloy plating bath, method of forming electrodeposits using the plating bath

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GB1089479A (en) * 1965-11-09 1967-11-01 Monsanto Chemicals Improvements relating to electrodeposition of tin
GB1339133A (en) * 1970-06-19 1973-11-28 Ciba Geigy Uk Ltd Tin plating additives and baths
US4073701A (en) * 1976-10-15 1978-02-14 Bethlehem Steel Corporation Acid electrotinning bath

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AU603790B2 (en) 1990-11-29
JPH07107198B2 (en) 1995-11-15
ATE119587T1 (en) 1995-03-15
KR940010459B1 (en) 1994-10-22
EP0241415A1 (en) 1987-10-14
ES2069532T3 (en) 1995-05-16
KR870009055A (en) 1987-10-23
AU7054487A (en) 1987-10-01
CA1336129C (en) 1995-07-04
DE3751126D1 (en) 1995-04-13

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