NO120248B - - Google Patents

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Publication number
NO120248B
NO120248B NO2638/69A NO263869A NO120248B NO 120248 B NO120248 B NO 120248B NO 2638/69 A NO2638/69 A NO 2638/69A NO 263869 A NO263869 A NO 263869A NO 120248 B NO120248 B NO 120248B
Authority
NO
Norway
Prior art keywords
aluminum
tin
alternating current
electrolyte
salt
Prior art date
Application number
NO2638/69A
Other languages
Norwegian (no)
Inventor
O Gedde
Original Assignee
O Gedde
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 O Gedde filed Critical O Gedde
Priority to NO2638/69A priority Critical patent/NO120248B/no
Priority to DE2025284A priority patent/DE2025284B2/en
Priority to NL707008252A priority patent/NL141580B/en
Priority to ES380638A priority patent/ES380638A1/en
Priority to FR7022404A priority patent/FR2047917B1/fr
Priority to AT547470A priority patent/AT298924B/en
Priority to SE08588/70A priority patent/SE357392B/xx
Priority to BE752359D priority patent/BE752359A/en
Priority to DK326970AA priority patent/DK131243B/en
Priority to CH953570A priority patent/CH554945A/en
Priority to FI701764A priority patent/FI46987C/en
Priority to US00049951A priority patent/US3849263A/en
Priority to GB3089070A priority patent/GB1311716A/en
Publication of NO120248B publication Critical patent/NO120248B/no

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Classifications

    • 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

Description

Fremgangsmåte ved elektrolytisk farving av aluminium som på forhånd er blitt anodisk oxydert. Process for electrolytic coloring of aluminum that has been anodically oxidized beforehand.

Oppfinnelsen angår en fremgangsmåte ved elektrolytisk farving The invention relates to a method of electrolytic dyeing

av aluminium eller aluminiumlegeringar som på forhånd er blitt anodisk oxydert. De ved fremgangsmåten oppnådde belegg har en- .jevn farve med god holdbarhet» of aluminum or aluminum alloys that have been anodically oxidized in advance. The coatings obtained by the method have a uniform color with good durability"

Det er for aluminium og aluminiumlegeringer, som for enkelhets skyld nedenfor også vil bli betegnet som aluminium, blitt utviklet en rekke farvemetoder. Den mest anvendte består i en neddypping av anodisk oxydert aluminium i en farveopplosning av anilinfarver. Ved denne neddyppingsmetode kan det også anvendes noen få uorganiske og halvorganiske farveopplosninger„ En neddypping i to på hverandre foigende uorganiske bad for å utfelle et farvet, uopploselig salt A number of coloring methods have been developed for aluminum and aluminum alloys, which for the sake of simplicity will below also be referred to as aluminium. The most widely used consists of dipping anodic oxidized aluminum into a color solution of aniline dyes. With this immersion method, a few inorganic and semi-organic dye solutions can also be used„ An immersion in two adjacent inorganic baths to precipitate a colored, insoluble salt

i oxydskiktet er også brukt. in the oxide layer is also used.

Det er også blitt utviklet fremgangsmåter basert på en såkalt integrert farveanodisering hvor farven utvikles av legeringselementer i aluminiumet samtidig med dannelsen av aluminiumoxydbelegget. Methods have also been developed based on a so-called integrated color anodization where the color is developed by alloying elements in the aluminum simultaneously with the formation of the aluminum oxide coating.

Det tas ved disse fremgangsmåter hele tiden sikte på å tilveie-bringe vakre og holdbare farver på aluminiumet for utendors bruk. With these methods, the aim is always to provide beautiful and durable colors on the aluminum for outdoor use.

De ovennevnte fremgangsmåter gir imidlertid enten for lite holdbare belegg eller belegg som er dyre å fremstille. However, the above-mentioned methods either provide coatings that are not very durable or coatings that are expensive to produce.

De seneste fremskritt er basert på elektrolytisk utfelling av farvede metallforbindelser i et på forhånd dannet aluminiumoxydskikt ved å lede vekselstrom mellom en aluminiumgjenstand og en annen elektrode i en sur elektrolytt inneholdende opploselige metallforbindelser. Således angår norsk patent nr. 69930 bruk av en sur elektrolytt inneholdende metallsalter av gruppen jern-, kobolt-, nikkel-, mangan- og/eller kromsalter sammen med små mengder av inntil 10 g/liter av en annen gruppe omfattende opploselige forbindelser av arsen, antimon, vismut, selen, tellur og/eller tinn. Det oppnåes med disse sammensatte elektrolytter forskjellige bronsetoner på aluminiumgjenstanden ved at farvede forbindelser av metallene jern, kobolt, nikkel og mangan derved lar seg innfore elektrolytisk i oxydskiktene. Det angis i patentet at innholdet av arsen, antimon, vismut, selen, tellur og/eller tinn ikke må overstige en bestemt grense for at det skal kunne opprettholdes en i praksis brukbar stromtetthet. The latest advances are based on electrolytic precipitation of colored metal compounds in a previously formed aluminum oxide layer by passing alternating current between an aluminum object and another electrode in an acidic electrolyte containing soluble metal compounds. Thus, Norwegian patent no. 69930 relates to the use of an acidic electrolyte containing metal salts from the group of iron, cobalt, nickel, manganese and/or chromium salts together with small amounts of up to 10 g/liter of another group comprising soluble compounds of arsenic , antimony, bismuth, selenium, tellurium and/or tin. With these compound electrolytes, different bronze tones are achieved on the aluminum object by the fact that colored compounds of the metals iron, cobalt, nickel and manganese can thereby be introduced electrolytically into the oxide layers. It is stated in the patent that the content of arsenic, antimony, bismuth, selenium, tellurium and/or tin must not exceed a certain limit in order to maintain a practically usable current density.

Britisk patent nr. 1022927 angår en fremgangsmåte hvor det for farving av en anodisk oxydertaluminiumgjenstand ledes en vekselstrom mellom denne og en motelektrode av carbon, carborundum eller aluminium i et vandig bad inneholdende et salt som gir et farvet metalloxyd eller -hydroxyd. Som metallsalter i elektrolytten er det foreslått å anvende små mengder av et salt av nikkel, kobolt, krom, kadmium? vanadium, gull, solv, jern eller bly. British patent no. 1022927 relates to a method where, for coloring an anodic oxidized aluminum object, an alternating current is passed between it and a counter electrode of carbon, carborundum or aluminum in an aqueous bath containing a salt which gives a colored metal oxide or hydroxide. As metal salts in the electrolyte, it is proposed to use small amounts of a salt of nickel, cobalt, chromium, cadmium? vanadium, gold, silver, iron or lead.

Fra tysk patent nr. 7<1>+1753 er det kjent elektrolytisk å farve gjenstander av på forhånd oxydert aluminium ved å lede vekselstrom gjennom et bad inneholdende opploste salter av metaller som er mer elektropositive enn aluminium, under anvendelse av en motelektrode bestående av det samme metall som metallet av det salt som er opplost i badet. De eneste metallsalter som er spesielt anfort som anvende-lige ved fremgangsmåten ifolge det tyske patent nr. 7^1.753» er From German Patent No. 7<1>+1753 it is known electrolytically to dye articles of previously oxidized aluminum by passing alternating current through a bath containing dissolved salts of metals more electropositive than aluminum, using a counter electrode consisting of the the same metal as the metal of the salt dissolved in the bath. The only metal salts which are specifically stated to be applicable in the process according to German Patent No. 71,753" are

kobber salter, nikkelsalter og solvsalter. copper salts, nickel salts and solar salts.

Det er en rekke metaller, deriblant tinn, som er mer elektropositive enn aluminium, men det er typisk for teknikkens stand at det ikke er blitt foreslått å anvende en elektrolytt inneholdende et opplost salt av tinn som det metall som skal gi farving av oxydskiktet til på forhånd anodisk oxyderte gjenstander av aluminium eller aluminiumlegeringer. There are a number of metals, including tin, which are more electropositive than aluminium, but it is typical of the state of the art that it has not been proposed to use an electrolyte containing a dissolved salt of tin as the metal which will give the color of the oxide layer to pre-anodically oxidized articles of aluminum or aluminum alloys.

Det har nu overraskende vist seg at det ved anvendelse av en elektrolytt inneholdende i det vesentlige bare tinnioner som metall-ioner kan oppnåes jevne, meget pene, farvede belegg på en på forhånd anodisk oxydert aluminiumgjenstand ved mellom denne og en motelektrode neddykket i elektrolytten å lede en vekselstrom. It has now surprisingly been shown that by using an electrolyte containing essentially only tin ions as metal ions, even, very attractive, colored coatings can be obtained on a previously anodically oxidized aluminum object by conducting between this and a counter electrode immersed in the electrolyte an alternating current.

Oppfinnelsen angår således en fremgangsmåte ved elektrolytisk farving av aluminium ved i en sur, vandig opplosning av et metallsalt å lede en vekselstrom mellom en på forhånd anodisk oxydert aluminiumgjenstand og en motelektrode fortrinnsvis bestående av tinn eller titan, og fremgangsmåten er særpreget ved at det som metallsalt anvendes et tinnsalt. The invention thus relates to a method for electrolytic coloring of aluminum by passing an alternating current in an acidic, aqueous solution of a metal salt between a previously anodically oxidized aluminum object and a counter electrode preferably consisting of tin or titanium, and the method is characterized by the fact that the metal salt a stannous salt is used.

Den ved foreliggende fremgangsmåte anvendte motelektrode er ikke av avgjorende betydning, men den bor fortrinnsvis være av tinn dersom det er onskelig kontinuerlig å erstatte de tinnioner i elektrolytten som forbrukes under farvingen, eller av et materiale som ikke an-gripes av elektrolytten, f.eks. rustfritt stål og titan, for å få The counter electrode used in the present method is not of decisive importance, but it should preferably be made of tin if it is desirable to continuously replace the tin ions in the electrolyte that are consumed during the dyeing, or of a material that is not attacked by the electrolyte, e.g. . stainless steel and titanium, to get

en elektrode med lang brukstid, og for å hindre forurensninger fra å tilfores elektrolytten. Den ved foreliggende fremgangsmåte anvendte motelektrode består fortrinnsvis av tinn eller titan. an electrode with a long service life, and to prevent impurities from being added to the electrolyte. The counter electrode used in the present method preferably consists of tin or titanium.

Foreliggende' fremgangsmåte kan utfores ved anvendelse av tinn-salter i en konsentrasjon av 0,5 - 20 %, fortrinnsvis ca. 2,0 %, basert på elektrolytten. Denne kan fortrinnsvis ha en pH av ca. 1,5. Vekselstrømmen kan være sinusformet eller ha annen kurveform og ha et periodetall av 10-500 perioder pr. sekund, fortrinnsvis 50 perioder pr. sekund, og en spenning av 2-50 V, fortrinnsvis 6 V, og det kan anvendes en stromtetthet av 0,2 - 0,8 A/dm^, basert på aluminiumg jenstanden. The present method can be carried out using tin salts in a concentration of 0.5 - 20%, preferably approx. 2.0%, based on the electrolyte. This can preferably have a pH of approx. 1.5. The alternating current can be sinusoidal or have a different curve shape and have a period number of 10-500 periods per second, preferably 50 periods per second, and a voltage of 2-50 V, preferably 6 V, and a current density of 0.2 - 0.8 A/dm^ can be used, based on the aluminum thickness.

EKSEMPEL 1 EXAMPLE 1

En aluminiumgjenstand som på forhånd var blitt anodisk oxydert An aluminum object that had previously been anodically oxidized

i en 15^ vandig opplosning av svovelsyre, ble forbundet med en motr elektrode av tinn i en vandig elektrolytt inneholdende 2 % tinn- in a 15% aqueous solution of sulfuric acid, was connected to a counter electrode of tin in an aqueous electrolyte containing 2% tin-

klorid og 50 ml konsentrert saltsyre pr. liter. En vekselspenning av 5-8 V ble ved værelsetemperatur tilfort elektrodene i en tid vari-erende fra 5-15 min, og den anvendte strømtetthet ble variert fra 0,2-0,8 A/dm 2 . Det ble oppnåodd meget pene bronsenyanser på aluminiumgjenstandene avhengig av varigheten av vekselstromtilforselen. Bronsenyansene ble dypere med tiltagende varighet av vekselstromtilforselen. chloride and 50 ml concentrated hydrochloric acid per litres. An alternating voltage of 5-8 V was applied to the electrodes at room temperature for a time varying from 5-15 min, and the applied current density was varied from 0.2-0.8 A/dm 2 . Very nice bronze shades were obtained on the aluminum objects depending on the duration of the alternating current supply. The bronze hues deepened with increasing duration of the alternating current supply.

EKSEMPEL 2 EXAMPLE 2

En aluminiumstrimmel som på forhånd var blitt anodisk oxydert i ^5 min i en 15 % vandig opplosning av svovelsyre, ble farvet elektrolytisk under anvendelse av vekselstrom, en motelektrode av rustfritt stål og en vandig elektrolytt inneholdende ^0 ml konsentrert HC1 og 2,7 % SnCl2 pr. liter. Den anvendte vekselspenning var 3 vqlt med et periodetall av 50, og dette ga en stromtetthet av 0,^ - 0,5 An aluminum strip which had previously been anodically oxidized for ^5 min in a 15% aqueous solution of sulfuric acid was dyed electrolytically using alternating current, a stainless steel counter electrode and an aqueous electrolyte containing ^0 ml of concentrated HCl and 2.7% SnCl2 per litres. The alternating voltage used was 3 vqlt with a period number of 50, and this gave a current density of 0.^ - 0.5

A/dm . Farvingen varte i 10 min, -og det ble oppnådd en meget til^ talende brunsort farve på aluminiumstrimmelen. A/dm. The coloring lasted for 10 minutes, and a very attractive brown-black color was achieved on the aluminum strip.

De oppnådde belegg hadde en meget jevn farve, og dette viser The coatings obtained had a very uniform colour, and this shows

at elektrolytten hadde en god spredningsevne. that the electrolyte had good dispersibility.

I motsetning til hva det var rimelig å vente seg, tok aluminiumgjenstandene ved de anvendte tider for vekselstromtilforselen ingen skade av den kiorholdige elektrolytt, og de farved beleggs holdbarhet overfor korrosjon var meget god efter at aluminiumgjenstandene var blitt skylt med vann og "forseglet" på kjent måte. Contrary to what was reasonable to expect, the aluminum objects at the times used for the alternating current supply were not damaged by the chlorine-containing electrolyte, and the durability of the colored coatings against corrosion was very good after the aluminum objects had been rinsed with water and "sealed" in known manner.

Claims (1)

Fremgangsmåte ved elektrolytisk farving av aluminium ved i en sur, vandig opplosning av et metallsalt å lede en vekselstrom mellom en på forhånd anodisk oxydert aluminiumgjenstand og en motelektrode fortrinnsvis bestående av tinn eller titan, karakterisert ved at det som metallsalt anvendes et tinnsalt.Process for electrolytic coloring of aluminum by passing an alternating current in an acidic, aqueous solution of a metal salt between a previously anodically oxidized aluminum object and a counter electrode preferably consisting of tin or titanium, characterized in that a tin salt is used as the metal salt.
NO2638/69A 1969-06-25 1969-06-25 NO120248B (en)

Priority Applications (13)

Application Number Priority Date Filing Date Title
NO2638/69A NO120248B (en) 1969-06-25 1969-06-25
DE2025284A DE2025284B2 (en) 1969-06-25 1970-05-23 Process for making colored aluminum articles
NL707008252A NL141580B (en) 1969-06-25 1970-06-05 PROCEDURE FOR THE ELECTROLYTIC COLORING OF PRE-ANODIC OXIDIZED ALUMINUM, AND COLORED OBJECTS THEREOF.
ES380638A ES380638A1 (en) 1969-06-25 1970-06-11 Process for electrolytically colouring of aluminium which has previously been anodically oxidized
FR7022404A FR2047917B1 (en) 1969-06-25 1970-06-18
AT547470A AT298924B (en) 1969-06-25 1970-06-18 Process for the electrolytic coloring of objects made of aluminum or an aluminum alloy
SE08588/70A SE357392B (en) 1969-06-25 1970-06-22
BE752359D BE752359A (en) 1969-06-25 1970-06-22 PROCESS FOR ELECTROLYTICALLY COLORING ALUMINUM OBJECTS THAT HAVE BEEN SUBJECT TO ANODIC OXIDATION
DK326970AA DK131243B (en) 1969-06-25 1970-06-24 Electrolytic dyeing process aluminum that has been previously anodic oxidized.
CH953570A CH554945A (en) 1969-06-25 1970-06-24 PROCESS FOR ELECTROLYTIC STAINING OF ANODIC OXIDIZED OBJECTS MADE OF ALUMINUM OR AN ALUMINUM ALLOY.
FI701764A FI46987C (en) 1969-06-25 1970-06-24 Procedure for electrolytic dyeing of aluminum, which has been oxidized in advance
US00049951A US3849263A (en) 1969-06-25 1970-06-25 Process for electrolytically colouring of aluminium which has previously been anodically oxidized
GB3089070A GB1311716A (en) 1969-06-25 1970-06-25 Process for electrolytically colouring an anodically oxidized aluminium or aluminium alloy article

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
NO2638/69A NO120248B (en) 1969-06-25 1969-06-25

Publications (1)

Publication Number Publication Date
NO120248B true NO120248B (en) 1970-09-21

Family

ID=19878994

Family Applications (1)

Application Number Title Priority Date Filing Date
NO2638/69A NO120248B (en) 1969-06-25 1969-06-25

Country Status (13)

Country Link
US (1) US3849263A (en)
AT (1) AT298924B (en)
BE (1) BE752359A (en)
CH (1) CH554945A (en)
DE (1) DE2025284B2 (en)
DK (1) DK131243B (en)
ES (1) ES380638A1 (en)
FI (1) FI46987C (en)
FR (1) FR2047917B1 (en)
GB (1) GB1311716A (en)
NL (1) NL141580B (en)
NO (1) NO120248B (en)
SE (1) SE357392B (en)

Families Citing this family (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AT324795B (en) * 1973-07-02 1975-09-25 Piesslinger Ind Baubedarf PROCESS AND COLORING ELECTROLYTE FOR COLORING GRAY OF ANODIC OXIDIZED OBJECTS MADE OF ALUMINUM OR ITS ALLOYS
CH581706A5 (en) * 1973-11-09 1976-11-15 Alusuisse
JPS5334107B2 (en) * 1974-04-23 1978-09-19
US4128460A (en) * 1976-09-13 1978-12-05 Daiwa Kasei Kenkyujo Kabushiki Kaisha Coloring by electrolysis of aluminum or aluminum alloys
DE2732668C2 (en) * 1977-07-20 1979-08-23 Langbein-Pfanhauser Werke Ag, 4040 Neuss Aluminum sheet baking pan and process for its manufacture
JPS55500501A (en) * 1978-06-28 1980-08-07
US4180443A (en) * 1978-06-28 1979-12-25 Reynolds Metals Company Method for coloring aluminum
US4179342A (en) * 1978-06-28 1979-12-18 Reynolds Metals Company Coating system method for coloring aluminum
IT1142650B (en) * 1981-12-31 1986-10-08 Grace Italiana Spa ALUMINUM ELECTRO-COLORING PLANT AND PROCESS
GB2129442B (en) * 1982-09-24 1986-05-21 Pilot Pen Co Ltd Colouring anodized aluminium or aluminium alloys
DE3824403A1 (en) * 1988-07-19 1990-01-25 Henkel Kgaa METHOD FOR ELECTROLYTIC METAL SALT COLORING OF ANODISED ALUMINUM SURFACES
US4931151A (en) * 1989-04-11 1990-06-05 Novamax Technologies Holdings Inc. Method for two step electrolytic coloring of anodized aluminum
DE4120415A1 (en) * 1991-06-20 1992-12-24 Henkel Kgaa MADE-UP TIN (II) SULFATE GRANULES FOR ELECTROLYTIC METAL SALT COLORING
US5538617A (en) * 1995-03-08 1996-07-23 Bethlehem Steel Corporation Ferrocyanide-free halogen tin plating process and bath
US5658529A (en) * 1996-03-13 1997-08-19 Johnson & Johnson Medical, Inc. Method of protecting and sterilizing aluminum surfaces on medical instruments
EP3421646A1 (en) 2017-06-29 2019-01-02 EMPA Eidgenössische Materialprüfungs- und Forschungsanstalt Colouring method of aluminium alloy member
EP4257659A3 (en) * 2022-04-04 2024-02-28 Samsung Electronics Co., Ltd. Etching composition, method of etching metal-containing film by using the same, and method of manufacturing semiconductor device by using the same

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE741753C (en) * 1940-04-13 1943-11-17 Langbein Pfanhauser Werke Ag Process for the electrolytic coloring of objects made of aluminum with an oxidic surface layer
US3382160A (en) * 1960-03-31 1968-05-07 Asada Tahei Process for inorganically coloring aluminum
US3227639A (en) * 1961-10-24 1966-01-04 Aluminum Co Of America Method of anodizing aluminum with electrolyte containing sulfophthalic acid
GB1173597A (en) * 1965-12-09 1969-12-10 Acorn Anodising Company Ltd Improvements in or relating to the Anodising of Aluminium and its Alloys.
GB1127160A (en) * 1965-12-27 1968-09-11 Sumitomo Chemical Co A method of producing a coloured anodic oxide film on aluminium

Also Published As

Publication number Publication date
FI46987B (en) 1973-05-02
CH554945A (en) 1974-10-15
SE357392B (en) 1973-06-25
US3849263A (en) 1974-11-19
ES380638A1 (en) 1972-10-01
FR2047917A1 (en) 1971-03-19
NL7008252A (en) 1970-12-29
AT298924B (en) 1972-05-25
DK131243B (en) 1975-06-16
DK131243C (en) 1975-11-17
BE752359A (en) 1970-12-01
FR2047917B1 (en) 1975-11-07
GB1311716A (en) 1973-03-28
DE2025284B2 (en) 1975-08-07
NL141580B (en) 1974-03-15
FI46987C (en) 1973-08-10
DE2025284A1 (en) 1971-01-14

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