US2867514A - Method of deoxidizing an aluminum surface - Google Patents

Method of deoxidizing an aluminum surface Download PDF

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Publication number
US2867514A
US2867514A US533903A US53390355A US2867514A US 2867514 A US2867514 A US 2867514A US 533903 A US533903 A US 533903A US 53390355 A US53390355 A US 53390355A US 2867514 A US2867514 A US 2867514A
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solution
fluoride
aluminum
acid
bath
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US533903A
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Jr Nelson J Newhard
James H Thirsk
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Henkel Corp
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Amchem Products Inc
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Priority to US533903A priority Critical patent/US2867514A/en
Priority to GB14299/56A priority patent/GB792739A/en
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    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C22/00Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
    • C23C22/05Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions
    • C23C22/06Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions using aqueous acidic solutions with pH less than 6
    • C23C22/34Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions using aqueous acidic solutions with pH less than 6 containing fluorides or complex fluorides
    • C23C22/37Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using aqueous solutions using aqueous acidic solutions with pH less than 6 containing fluorides or complex fluorides containing also hexavalent chromium compounds
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C22/00Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
    • C23C22/73Chemical surface treatment of metallic material by reaction of the surface with a reactive liquid, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals characterised by the process
    • C23C22/77Controlling or regulating of the coating process
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23GCLEANING OR DE-GREASING OF METALLIC MATERIAL BY CHEMICAL METHODS OTHER THAN ELECTROLYSIS
    • C23G1/00Cleaning or pickling metallic material with solutions or molten salts
    • C23G1/02Cleaning or pickling metallic material with solutions or molten salts with acid solutions
    • C23G1/12Light metals
    • C23G1/125Light metals aluminium

Definitions

  • Our improved material consists essentially of an acid aqueous solution having a pH of between 0.5 and 1.0 and containing as its principal and essential ingredients hexavalent chromium and dissolved fluoride in certain proportions as will appear below.
  • hexavalent chromium in the solution With respect to the content of hexavalent chromium in the solution, we have found that this should lie between l and 100 grams per liter. Below grams per liter the bath may tend to produce a conversion coating on the surface of aluminum which will interfere with the action of the subsequently applied regular coating producing bath. In general, we have found that optimum results have been secured where the content of hexavalent chromium per liter ranges somewhere between and grams per liter. The source of the hexavalent chromium appears to make little or no difference. For in- Patented Jan. 6, 1959 Chromic acid grams 30 Hydrofiuoric acid (48.8%) rnilliliters 0.25 Water, to make 1 liter.
  • the source of fluoride may be hydrofluoric acid, simple salts such as sodium fluoride, ammonium fluoride, potassium fluoride, etc., or complex fluoride acid, such as fluoboric, fluosilicic or their soluble salts, such as sodium silica fluoride, potassium fluosilicate, ammonium silica fluoride, etc.
  • complex fluorides such as fluoboric, fluosilicic or their soluble salts, such as sodium silica fluoride, potassium fluosilicate, ammonium silica fluoride, etc.
  • the pH of the bath must be between 0.5 and 1.0 and, if desired, this pH may be secured in preparing the operating solution by adjusting the type and proportionate content of fluoride and chromate so that the desired degree of acidity is secured. However, where this is not done the acidity of the bath may be secured by addition of a small amount of nitric acid. In general, large quantities of sulfate and chloride ions are to be avoided.
  • the solutions of the present invention may be used at practically any temperature although, in most instances, we prefer to employ the temperature of the room in which the operation is carried out, say, somewhere between 50 and F.
  • the usual rule applies, namely, that the time of treatment may be shortened by elevation of the temperature or lengthened by a lowering of the temperature although between 50 and 90 F., as stated, the time element is not of too much importance.
  • most alloys of aluminum can be satisfactorily deoxidized in from one to two minutes unless the surface bear an excessively heavy oxide film when as much as two to four minutes may be required.
  • Suitable but not necessarily limiting examples of useful aluminum deoxidizing baths are as follows:
  • the metal should first be cleaned and this cleaning can be accomplished by any conventional means such as the use of a solvent, a mild alkali, etc.
  • the solution either by spraying or flowing the solution over the surface of the metal or by dipping the metal into a bath of the solution.
  • the solution should be allowed to act upon the surface until deoxidization of the surface has occurred which may take place in a period of from approximately one to four minutes, as indicated above, where the temperature of the bath lies between'SO and 90 F.
  • the metal is removed from further contact with the solution and is thereafter given a protective coating with any of the conventional fiuoride-chromate coating solutions familiar to the art, as mentioned near the beginning of this disclosure.
  • fluoride is supplied from the, class of ,fluorideswhich consists of complex fluoride acids and soluble salts thereof.
  • aqueous acid solution consisting essentially of hexavalent chromium and fluoride, the quantity of hexavalent chromium being from 10 to .100 grams per liter and the quantity of fluoride being suflicient to give a bath activity at least as great as a solution of:

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)
  • Chemical Treatment Of Metals (AREA)

Description

METHOD OF DEOXIDIZING AN ALUMINUM SURFACE Nelson J. Newhard, Jr., Oreland, and James H. Thirsk, Meadowbrook, Pa., assignors to Amchem Products, Inc., a corporation of Delaware No Drawing. Application September 12, 1955 Serial N0. 533,903
4 Claims. (Cl. 41-42) This invention relates to the art of treating metallic surfaces and is particularly concerned with the provision of an improved metal treating material and an improved method for deoxidizing surfaces of aluminum. For purposes of exemplification, the following disclosure will be directed to the treatment of aluminum and in this connection it should be understood that the word aluminum as used herein includes not only essentially pure aluminum but also such alloys thereof in which aluminum is the principal ingredient.
As is well known, upon exposure to air, aluminum surfaces tend to oxidize. Such an oxidized surface presents certain. problems when it is desired to apply to the surface a corrosion resistant coating by treating it with known .acidic solutions consisting principally of hexavalentchromiumand fluorides with or without special additives for special purposes. For instance, if a uniform coating is to be produced by employing such an acidic solution, it is necessary to deoxidize the aluminum surface prior to subjecting it to the action of the coating solution. Unfortunately, the deoxidizing solutions heretofore employed, while removing the oxide film tend to objectionably etch the surface of the aluminum and, for some reason not fully understood by the inventors, quite often lead to an impairment of the corrosion resistance of the subsequently coated surface when contrasted with the corrosion resistance that can be secured by coating the surface without deoxidizing it.
We have found it possible to deoxidize aluminum surfaces which, in whole or in part, bear an oxide film without producing a heavy etch and without any apparent impairment in the corrosion resistance of the subsequently coated surface.
With the foregoing in mind, the principal objects of our invention may be stated as involving the provision of "an improved metal treating material and a novel method by means of which an aluminum surface may be satisfactorily deoxidized without producing thereon a heavy etch and without impairment of the corrosion resistance of the surface when subsequently coated by the familiar acidic solutions of the art which consist primarily of hexavalent chromium and fluorides.
Our improved material consists essentially of an acid aqueous solution having a pH of between 0.5 and 1.0 and containing as its principal and essential ingredients hexavalent chromium and dissolved fluoride in certain proportions as will appear below.
With respect to the content of hexavalent chromium in the solution, we have found that this should lie between l and 100 grams per liter. Below grams per liter the bath may tend to produce a conversion coating on the surface of aluminum which will interfere with the action of the subsequently applied regular coating producing bath. In general, we have found that optimum results have been secured where the content of hexavalent chromium per liter ranges somewhere between and grams per liter. The source of the hexavalent chromium appears to make little or no difference. For in- Patented Jan. 6, 1959 Chromic acid grams 30 Hydrofiuoric acid (48.8%) rnilliliters 0.25 Water, to make 1 liter.
and B Chromic acid grams 30 Hydrofiuoric acid (48.8%) milliliters 0.25
Water, to make 1 liter.
Should the fluoride activity of the bath be less than the activity of Solution A the bath will not deoxidize properly. Conversely, if the bath activity is greater than the activity of solution B, there will be a tendency of the bath to undesirably etch the aluminum surface. In order to determine the activity of the bath, it has been-found desirable and convenient to use ordinary commercial microscope slides of lime-soda glass. It has been found convenient to meaure the activity of the bath by heating a convenient volume to approximately 120 F. and immersing enough microscope slides as is necessary to se cure 26 square inches of surface in the solution for two hours and measuring the weight loss of the glass at the end of the two hour immersion. Obviously, the measurements with solutions A and B are made under similar conditions.
The source of fluoride may be hydrofluoric acid, simple salts such as sodium fluoride, ammonium fluoride, potassium fluoride, etc., or complex fluoride acid, such as fluoboric, fluosilicic or their soluble salts, such as sodium silica fluoride, potassium fluosilicate, ammonium silica fluoride, etc. As a general rule, we prefer to use the complex fluorides as a source of fluoride because when so doing optimum results seem to be achieved.
The pH of the bath must be between 0.5 and 1.0 and, if desired, this pH may be secured in preparing the operating solution by adjusting the type and proportionate content of fluoride and chromate so that the desired degree of acidity is secured. However, where this is not done the acidity of the bath may be secured by addition of a small amount of nitric acid. In general, large quantities of sulfate and chloride ions are to be avoided.
Insofar as temperatures are concerned, the solutions of the present invention may be used at practically any temperature although, in most instances, we prefer to employ the temperature of the room in which the operation is carried out, say, somewhere between 50 and F. The usual rule applies, namely, that the time of treatment may be shortened by elevation of the temperature or lengthened by a lowering of the temperature although between 50 and 90 F., as stated, the time element is not of too much importance. Within that range, most alloys of aluminum can be satisfactorily deoxidized in from one to two minutes unless the surface bear an excessively heavy oxide film when as much as two to four minutes may be required.
Suitable but not necessarily limiting examples of useful aluminum deoxidizing baths are as follows:
Example No. I
Grams Example No. II i Grams Chromic acid 40 Hydrofluoric acid, 100% basis 0.12 Water, to make 1 liter. 1'
Example N0. III
Water, to make 1 liter.
NOTE.-Th6 pH of this bath is adjusted to 0.85 with nitric acid.
In employing our improved solutions for the deoxidiz ation of aluminum surfaces, the metal should first be cleaned and this cleaning can be accomplished by any conventional means such as the use of a solvent, a mild alkali, etc.
solution either by spraying or flowing the solution over the surface of the metal or by dipping the metal into a bath of the solution. The solution should be allowed to act upon the surface until deoxidization of the surface has occurred which may take place in a period of from approximately one to four minutes, as indicated above, where the temperature of the bath lies between'SO and 90 F.
After the deoxidizing action has been completed the metal is removed from further contact with the solution and is thereafter given a protective coating with any of the conventional fiuoride-chromate coating solutions familiar to the art, as mentioned near the beginning of this disclosure.
We claim: 1. The method of treating an aluminum surface which After the cleaning operation the surface of the metal is brought into contact with the deoxidizing Grams Potassium dichromate ,90 Potassium zirconium fluoride 1.2
fluoride is supplied from the, class of ,fluorideswhich consists of complex fluoride acids and soluble salts thereof.
consists in subjecting the surface'to the action of an aqueous acid solution consisting essentially of hexavalent chromium and fluoride, the quantity of hexavalent chromium being from 10 to .100 grams per liter and the quantity of fluoride being suflicient to give a bath activity at least as great as a solution of:
Chromic acid Q. grams 30 48.8% hydrofluoric acid "milliliters" 0.25 Water, to make 1 liter.
but having no more activity than a solution of; Chromic acid g ams-.. 30
48.8% hydrofluoric acid mi1liliter s 1 Water, to make 1 liter.
References Cited in the file of this patent UNITED STATES PATENTS 716,977 Anderson Dec. 30, 1902 7 2,357,991 Ayers Sept. 12, 1944 2,593,448 Hesch Apr. 22, 71 952 2,613,165 Fischer Oct. 7., 1 952 Floersch Oct. 13, 19,53
UIHTED S ATES PATENT UFFICE csrmmrr r QQRECM Patent No, 2,867,514 January 6, 195
Nelson J, Newhard, Jr. et al.
It is hereby certified that error appears in the -printed specification of the above numbered patent requiring correction and that the said Letters Patent should read as corrected below.
Column 2, line 16, for rnilliliteraj.25 read M milliliters laO line 61, for "surface" read M surface-s m Signed and sealed this 14th day of April 1959u (SEAL) Attest:
K R u AXLINE ROBERT C. WATSON Attesting Officer Commissioner of Patents Unirnn STATES PATENT OFFICE QERTIFIQATE F QQEQTION Patent No 2,867,514
Nelson J Newhard, Jr.,, et ,al,
It is hereby certified that error appears in the-printed specification of the above numbered patent requiring correction and that the said Letters Patent should read as corrected below.
Column 2, line 16, for milliliters G.25" read milliliterswLO line 61, for "SUI'faCG" read surfaces o Signed and sealed this 14th day of April 1959c l: SEAL) Attest:
KARL AXLINE ROBERT C. WATSON Commissioner of Patents Attesting Oificer January 6, 1959

Claims (1)

1. THE METHOD OF TREATING AN ALUMINUM SURFACE WHICH CONSISTS IN SUBJECTING THE SURFACE TO THE ACTION OF AN AQUEOUS ACID SOLUTION CONSISTING ESSENTIALLY OF HEXAVALENT CHROMIUM AND FLORIDE, THE QUANTITY OF HEXVALENT CHROMIUM BEING FROM 10 TO 100 GRAMS PER LITER AND THE QUANTITY OF FLUORIDE BEING SUFFICIENT TO GIVE A BATH ACTIVITY AT LEAST AS GREAT AS A SOLUTION OF: CHROMIC ACID GRAMS 30 48.8% HYDROFLUORIC ACID MILLILTERS 0.25 WATER, TO MAKE 1 LITER BUT HAVING NO MORE ACTIVITY THAN A SOLUTION OF: CHROMIC ACID GRAMS 30 48.8% HYDROFLUORIC ACID MILLILTERS 1 WATER, TO MAKE 1 LITER. THE PH OF THE SOLUTION BEING BETWEEN 0.5 AND 1.0. AND THE TREATMENT BEING CONTINUED UNTIL THE SURFACE IS DEOXIDIZED.
US533903A 1955-09-12 1955-09-12 Method of deoxidizing an aluminum surface Expired - Lifetime US2867514A (en)

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Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3074824A (en) * 1962-03-16 1963-01-22 Aluminum Co Of America Removing flux residues
US3108919A (en) * 1959-06-17 1963-10-29 North American Aviation Inc Etching process
US3239440A (en) * 1964-11-23 1966-03-08 Titanium Metals Corp Electrolytic pickling of titanium and titanium base alloy articles
US3367799A (en) * 1963-10-08 1968-02-06 Army Usa Process for cleaning aluminum
US3645790A (en) * 1969-02-17 1972-02-29 Hooker Chemical Corp Composition and process for cleaning metal
US4087367A (en) * 1974-10-18 1978-05-02 U.S. Philips Corporation Preferential etchant for aluminium oxide
FR2550551A1 (en) * 1983-08-12 1985-02-15 Nippon Light Metal Co PROCESS FOR HYDROPHILIC SURFACE TREATMENT OF ALUMINUM OBJECTS AND PRODUCTS THUS OBTAINED
US4851077A (en) * 1988-05-19 1989-07-25 Mcdonnell Douglas Corporation Chemical milling of lithium aluminum alloy
US5052421A (en) * 1988-07-19 1991-10-01 Henkel Corporation Treatment of aluminum with non-chrome cleaner/deoxidizer system followed by conversion coating
US5227016A (en) * 1992-02-25 1993-07-13 Henkel Corporation Process and composition for desmutting surfaces of aluminum and its alloys
US20150040799A1 (en) * 2013-08-07 2015-02-12 The Boeing Company Reduction of chromium waste water in an aluminum conversion coat processing line
CN105624700A (en) * 2015-12-29 2016-06-01 浙江师范大学 Acid adhesive removing agent for aluminum alloys as well as preparation method and application of acid adhesive removing agent

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US716977A (en) * 1901-07-27 1902-12-30 John A Gilliam Process of purifying aluminium.
US2357991A (en) * 1941-11-12 1944-09-12 Wingfoot Corp Treatment of magnesium
US2593448A (en) * 1949-07-25 1952-04-22 Kaiser Aluminium Chem Corp Method and composition for treating aluminum and aluminum alloys
US2613165A (en) * 1950-07-03 1952-10-07 Aluminum Co Of America Surface treatment of magnesium and magnesium alloy articles
US2655439A (en) * 1952-12-15 1953-10-13 Ryan Aeronautical Co Compounded fluoborate chemical surface treatment of aluminum and aluminum alloys

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US716977A (en) * 1901-07-27 1902-12-30 John A Gilliam Process of purifying aluminium.
US2357991A (en) * 1941-11-12 1944-09-12 Wingfoot Corp Treatment of magnesium
US2593448A (en) * 1949-07-25 1952-04-22 Kaiser Aluminium Chem Corp Method and composition for treating aluminum and aluminum alloys
US2613165A (en) * 1950-07-03 1952-10-07 Aluminum Co Of America Surface treatment of magnesium and magnesium alloy articles
US2655439A (en) * 1952-12-15 1953-10-13 Ryan Aeronautical Co Compounded fluoborate chemical surface treatment of aluminum and aluminum alloys

Cited By (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3108919A (en) * 1959-06-17 1963-10-29 North American Aviation Inc Etching process
US3074824A (en) * 1962-03-16 1963-01-22 Aluminum Co Of America Removing flux residues
US3367799A (en) * 1963-10-08 1968-02-06 Army Usa Process for cleaning aluminum
US3239440A (en) * 1964-11-23 1966-03-08 Titanium Metals Corp Electrolytic pickling of titanium and titanium base alloy articles
US3645790A (en) * 1969-02-17 1972-02-29 Hooker Chemical Corp Composition and process for cleaning metal
US4087367A (en) * 1974-10-18 1978-05-02 U.S. Philips Corporation Preferential etchant for aluminium oxide
FR2550551A1 (en) * 1983-08-12 1985-02-15 Nippon Light Metal Co PROCESS FOR HYDROPHILIC SURFACE TREATMENT OF ALUMINUM OBJECTS AND PRODUCTS THUS OBTAINED
US4851077A (en) * 1988-05-19 1989-07-25 Mcdonnell Douglas Corporation Chemical milling of lithium aluminum alloy
US5052421A (en) * 1988-07-19 1991-10-01 Henkel Corporation Treatment of aluminum with non-chrome cleaner/deoxidizer system followed by conversion coating
US5227016A (en) * 1992-02-25 1993-07-13 Henkel Corporation Process and composition for desmutting surfaces of aluminum and its alloys
US20150040799A1 (en) * 2013-08-07 2015-02-12 The Boeing Company Reduction of chromium waste water in an aluminum conversion coat processing line
US9683293B2 (en) * 2013-08-07 2017-06-20 The Boeing Company Reduction of chromium waste water in an aluminum conversion coat processing line
US10472720B2 (en) 2013-08-07 2019-11-12 The Boeing Company Reduction of chromium waste in an aluminum conversion coat processing line
CN105624700A (en) * 2015-12-29 2016-06-01 浙江师范大学 Acid adhesive removing agent for aluminum alloys as well as preparation method and application of acid adhesive removing agent
CN105624700B (en) * 2015-12-29 2018-05-25 浙江师范大学 A kind of acidity aluminium alloy adhesive remover and its preparation method and application

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