US3060071A - Process of treating zinc castings - Google Patents

Process of treating zinc castings Download PDF

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US3060071A
US3060071A US676514A US67651457A US3060071A US 3060071 A US3060071 A US 3060071A US 676514 A US676514 A US 676514A US 67651457 A US67651457 A US 67651457A US 3060071 A US3060071 A US 3060071A
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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
    • C23FNON-MECHANICAL REMOVAL OF METALLIC MATERIAL FROM SURFACE; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL; MULTI-STEP PROCESSES FOR SURFACE TREATMENT OF METALLIC MATERIAL INVOLVING AT LEAST ONE PROCESS PROVIDED FOR IN CLASS C23 AND AT LEAST ONE PROCESS COVERED BY SUBCLASS C21D OR C22F OR CLASS C25
    • C23F3/00Brightening metals by chemical means
    • C23F3/04Heavy metals
    • C23F3/06Heavy metals with acidic solutions

Definitions

  • a primary object of this invention is to produce a bright corrosion-resistant surface on zinc casings by a simple chemical treatment, such as by dipping or immersion.
  • Another object of this invention is to provide a bright surface on zinc castings and then plating over such surface with copper or nickel or chromium, thus eliminating the cost of buffing, burnishing, etc.
  • An equally important object of this invention is to provide an aqueous acidic chromate solution for obtaining a bright chemically polished surface on zinc castings such as sand and die castings, and provide the same with a clear, corrosion-protective, chromate conversion coating.
  • Such coating is also useful as a final finish or as a base for paint and the usual electroplated deposits, such as acid fluorides of metals may be substituted in quantifies to provide an equivalent fluoride concentration, e.g., KF, potassium fluoride, for which sodium or ammonium fluorides may be substituted as above, HF, hydrofluoric acid concentration to 60% by Weight, preferably 60% by weight, sp. gr.
  • HNO nitric acid preferably 61.4% by Weight, sp. gr. 1.38, but commercial concentrations of from 58% to 72% have been used in the various examples successfully
  • H SO sulfuric acid preferably 93.5% by weight, sp. gr. 1.84 but commercial grades from 60% to 93.5% have been successfully used in the various examples
  • HAc, acetic acid, glacial, 99.5 sp gr. 1.05, but 80% to 99.5% have been successfully used in various examples
  • the concentrations are, of course, expressed in aqueous solution.
  • Example Example Example Example 2 3 4 5 6 copper, nickel or chromium.
  • the bright surface coat ing, with or without the subsequent electroplated coatings, will preclude the need for hand buffing or substantially lessen the necessity for conventional finishing treatments.
  • the solutions of this invention attack the metal sufficiently to produce chemical polishing without leaving a smut.
  • a chromate surface conversion coating is deposited on the metal at the same time. This coating varies from an extremely thin type which is practically invisible to a thicker coating having a pronounced yellow color.
  • the coatings of this invention have a generally higher degree of corrosion protection than similar coatings from solutions formulated for use on pure zinc only.
  • Acetic acid is used where necessary for control of the thickness of the coatings, particularly when the time between removal of the work from the chemical polishing bath and its immersion in the succeeding water rinse is greater than 15 seconds. 'The upper and lower limits of the ranges recited in the foregoing Examples 1 to 7, as well as intermediate amounts of the constituents, have been successfully used.
  • the zinc casting treated is first cleaned in the usual manner with a conventional alkaline cleaner for zinc die castings, preferably by dipping in the cleaning bath, the immersion time being about 10 to 30 seconds and the solution preferably being at elevated temperature; then the cleaned castings are hot or cold rinsed in water thoroughly and introduced into one of the dips of this invention, the temperature of the dips being between F. and 160-F., preferably about F. and the immersion time being from about 5 seconds to 2 minutes, preferably about 30 seconds; then the treated castings are hot or cold water rinsed and dried in a conventional manner as by blowing warm air over the same or passing the castings through a drying chamber.
  • a conventional alkaline cleaner for zinc die castings preferably by dipping in the cleaning bath, the immersion time being about 10 to 30 seconds and the solution preferably being at elevated temperature; then the cleaned castings are hot or cold rinsed in water thoroughly and introduced into one of the dips of this invention, the temperature of the dips being between F. and 160-F., preferably about F. and the immersion time being
  • compositions and treatment of this invention as well as
  • Zamac #3 Alloys composed of zinc about 96% and aluminum 4%
  • Zamac gr. of 1.84 the sp. gr. of acetic acid was 1.05 and the concentration 99.5% by weight
  • the concentration of hydrochloric acid was 31.5% by weight, with a sp. gr. of 1.16, the concentrations being recited in terms of aqueous #5 Alloys composed approximately of zinc 96%, alumi- 5 solution. num 3.8% and copper 2%.
  • the ranges recited above relative to temperature of the TABLE 2 bath and time of immersion or treatment were successfully used and the amounts of these acids with the ranges of Formulas for Zama? #3 concentrations recited were also used successfully.
  • Examples 8, 9 and 10 are solutions which may be safely This example was like Example except that it was used to produce a bright surface on Zamac #3 di a tearned out with 40 milliliters of nitric ac1d instead of 80 ings. The treatment is followed by water rinsing and a milliliters, as reclted 111 Exampl conventional bleaching dip in a dilute solution of sodium hydroxide to remove the yellow constituents in the coating EXAMPLE 23 and leave a clear bright surface as a final finish.
  • Example 12 is a solution which contains the constituents in the proportions in which they are depleted in EXAMPLE 24 normal operation. It is intended for use in replenishing 110-180 g./1. C103 bower solutions such as Example 8 and is not itself suitable for ffi y lfgg use alone in performing the functions of this invention. 50410 mL/l. HNO
  • Examples 13, 14 and 15 perform the same functions for EXAMPLE 25 Zamac #5 as is performed for Za-mac #3 by Examples 8, 9 and 10, namely, chemical polishing for a clear bright final finish or in preparation 'for subsequent plating. If the sodium hydroxide or other bleaching dip is omitted, Example 15 may be used for a yellow final finish.
  • Example 16 is a solution for maintaining the solutions ofrExamples 13, 14 and 15 in opera-ting condition and corresponds to Example 12.
  • Examples 17 and 18 are for applying a thin, light yellow coating on die castings with a minimum of attack on the metal and, therefore, a minimum consumption of chemicals.
  • Examples 19 and 20 are adapted for use with either Zamac #3 or Zamac #5.
  • Example 20 which is formulated to operate at about 80 F.
  • the higher concentration of the fluoride salt in this example makes this possible.
  • the concentration of hydrofluoric acid was 60% by weight, with a sp. gr. of 1.24, the concentration of the nitric acid was 61.4% by weight, with a sp. gr. of 1.38, the sp. gr. of sulfuric acid was 93.5% by weight, with a sp.
  • HNOa Formulas 24 and 25 may be sold as a powder and the user will add the required amount of HNO EXANCPLE 26
  • Example 26 will be sold either-with or without the HNO
  • the following formulation was used on Zamac #3 castings which were then given conventional electroplating coatings of copper, chromium and nickel, respective- EXAMPLE 2? 99 g./l. CrO
  • the dip temperature as with the other examples recited above, was 140 F. and the immersion time was 30 seconds.
  • Example 27 is used prior to conventional electroplating with copper, chromium or nickel and the castings, both before and after electroplating, have an appearance of being hand buffed or polished, more so, however, when electroplated.
  • EXAMPLE 28 This formulation was used on a Zamae #5 casting (96% zinc, 3.8% aluminum and 2% copper) to give a semi-polish or bright yellow finish:
  • the temperature of the coating bath was 140 F. and immersion time seconds.
  • Example 29 In addition to the replenishing baths referred to above, Example 8 for illustration, as well as Examples 10 and 11 and other of the examples, Was fortified or replenished, i.e., maintained, from time to time to economically increase its operating life by adding to it and preferably to the baths for Zamac castings of Examples 1 to 27, notably Examples 6, 10 and 27, the following formulations:
  • EXAMPLE 30 150 g./l. CI'O 150 rnL/l. HNO 5 ml./l. H SO 30 ml. /l. HAc 40 g./l. NH HF 30 ml./l. HCl
  • one basic formula for a bright protective finish comprises about: 120 g./l. CrO 40 g./l. NH HF 50 ml./l. HNO
  • a preferred formulation for Zamac #3 castings comprises:
  • the CrO content is varied as indicated from about 30 g./l. upward.
  • the concentration of the acetic acid will vary between 0 to 100 ml./l., preferably 15 to 50 ml./l.; of the nitric acid between about 4 and 80 ml./l., preferably 4 to 60 ml./ 1.; of the sulfuric acid between about 0.1 to 10 ml./l., preferably 2 to 8 ml./l.; and of the hydrochloric acid between about 0 to 50 ml./l., preferably about 3 to 40 ml./l.
  • the bath temperatures successivefully used with the formulations of this application vary between F. and 160 F. but preferably F. is used. Also, I have used time periods of treatment from 5 seconds to 2 minutes with the various formulations but prefer a treatment of about 30 seconds.
  • ammonium bifluoride is preferred, sodium fluoride and other fluorides of equivalent or greater solubility may be used as indicated in the foregoing examples.
  • the process of treating zinc castings comprising immersing the same in an aqeueous acidic chromate bath containing CrO at least about 30 -g./ 1., and about 5 to 60 ml./l. I-INO 0 to 100 mL/l HAc, 2 to 10 ml./l. H SO and 4 to 50 g./l. of a soluble fluoride, for from 5 seconds "contains 3 to 40 BIL/1. HQ.
  • the process of treating zinc castings comprising immersing the same in an aqueous acidic chromate bath containing CrO about 99 g./l., and about 5 to 60 m1./l. HNO 0 to 100 ml./l. HAc, 2 to mL/l. H 80 and 4 to 50 -g./l. of a soluble fluoride, for from 5 seconds to 2 minutes with the bath at a temperature between about 110 F. and 160 F.
  • the process of treating zinc castings comprising immersing the same in an aqueous acidic chromate bath containing CrO about 120 g./l., and about 5 to 60 ml./l. HNO 0 to 100 -m1./ l. HAc, 2 to 10 ml./-l. H 50 and 4 to 50 g./1. of a soluble fluoride, for from 5 seconds to 2 minutes with the bath at a temperature between about 110 F. and 160 F.

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  • Chemical & Material Sciences (AREA)
  • General Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Chemical Treatment Of Metals (AREA)
  • ing And Chemical Polishing (AREA)

Description

United States Patent 3,060,071 PROCESS OF TREATING ZINC CASTINGS David H. Kinder, Baltimore, Md., assignor to Allied Research Products Incorporated, Baltimore, Md, a corporation of Maryland No Drawing. Filed Aug. 6, 1957, Ser. No. 676,514- 9 Claims. (Cl. 156-18) This invention relates to an improved acidic chromate solution for providing chemical polishing of zinc die cast surfaces with the additional advantages of forming a film which will protect against corrosion.
A primary object of this invention is to produce a bright corrosion-resistant surface on zinc casings by a simple chemical treatment, such as by dipping or immersion.
Another object of this invention is to provide a bright surface on zinc castings and then plating over such surface with copper or nickel or chromium, thus eliminating the cost of buffing, burnishing, etc.
An equally important object of this invention is to provide an aqueous acidic chromate solution for obtaining a bright chemically polished surface on zinc castings such as sand and die castings, and provide the same with a clear, corrosion-protective, chromate conversion coating. Such coating is also useful as a final finish or as a base for paint and the usual electroplated deposits, such as acid fluorides of metals may be substituted in quantifies to provide an equivalent fluoride concentration, e.g., KF, potassium fluoride, for which sodium or ammonium fluorides may be substituted as above, HF, hydrofluoric acid concentration to 60% by Weight, preferably 60% by weight, sp. gr. 1.24, but commercial grades of hydrofluoric acid, namely, 48% to 52% have been successfuly used in the various examples, HNO nitric acid, preferably 61.4% by Weight, sp. gr. 1.38, but commercial concentrations of from 58% to 72% have been used in the various examples successfully, H SO sulfuric acid, preferably 93.5% by weight, sp. gr. 1.84 but commercial grades from 60% to 93.5% have been successfully used in the various examples, HAc, acetic acid, glacial, 99.5 sp gr. 1.05, but 80% to 99.5% have been successfully used in various examples, and HCl, hydrochloric acid, sp. gr. 1.16, 31.5%, but concentrations of 24.6% to 35.2% have been successfully used in the various examples. The concentrations are, of course, expressed in aqueous solution.
The values for all dry materials, namely, CrO NH HF NaF and RF in the tables represent grams of compound per liter of aqueous solution, while the values of hydrofluoric acid, nitric acid, sulfuric acid, hydrochloric acid and acetic acid, namely, liquid materials, are represented in the various tables as milliliters of liquid per liter of aqueous solution.
TABLE 1 General Formulas Example Example Example Example Example 2 3 4 5 6 copper, nickel or chromium. The bright surface coat ing, with or without the subsequent electroplated coatings, will preclude the need for hand buffing or substantially lessen the necessity for conventional finishing treatments.
All previous solutions and compounds suitable for producing chromate surface conversion coating on zinc plate, galvanized metal, etc. have one of two efliects on zinc die castings. In one case, the bath has an almost negligible attack on the metal and a protective film is deposited without the occurrence of any chemical polishing or brightening. On the other hand, if the attack is appreciable, the aluminum and other alloying constituents are dissolved more slowly than the zinc and the surfaces are etched and left with a dark gray smut of undissolved material.
The solutions of this invention attack the metal sufficiently to produce chemical polishing without leaving a smut. A chromate surface conversion coating is deposited on the metal at the same time. This coating varies from an extremely thin type which is practically invisible to a thicker coating having a pronounced yellow color. The coatings of this invention have a generally higher degree of corrosion protection than similar coatings from solutions formulated for use on pure zinc only.
'In the three tables which follow, examples useful in carrying out the aims of this invention are shown. The materials used are as follows: CrO chromic acid anhydride, NH4HF2, ammonium acid fluoride, for which the Examples 1 through 7 illustrate ranges ofrconcentrations based on the use of chromic acid anhydride with a fluoride and a high concentration of hydrogen ion furnished by a mineral acid, for example, nitric acid. Sulfate ions from sulfuric acid and/ or chloride ions from hydrochloric acid are used in some solutions for their catalytic eifect in speeding the reaction. Acetic acid is used where necessary for control of the thickness of the coatings, particularly when the time between removal of the work from the chemical polishing bath and its immersion in the succeeding water rinse is greater than 15 seconds. 'The upper and lower limits of the ranges recited in the foregoing Examples 1 to 7, as well as intermediate amounts of the constituents, have been successfully used.
In the various examples recited throughout this specification, the zinc casting treated is first cleaned in the usual manner with a conventional alkaline cleaner for zinc die castings, preferably by dipping in the cleaning bath, the immersion time being about 10 to 30 seconds and the solution preferably being at elevated temperature; then the cleaned castings are hot or cold rinsed in water thoroughly and introduced into one of the dips of this invention, the temperature of the dips being between F. and 160-F., preferably about F. and the immersion time being from about 5 seconds to 2 minutes, preferably about 30 seconds; then the treated castings are hot or cold water rinsed and dried in a conventional manner as by blowing warm air over the same or passing the castings through a drying chamber.
The compositions and treatment of this invention, as
stated, are primarily useful in connection with imparting a brightness to zinc die castings, notably, for such products as are known in the trade as Zamac #3 Alloys composed of zinc about 96% and aluminum 4%, and Zamac gr. of 1.84, the sp. gr. of acetic acid was 1.05 and the concentration 99.5% by weight, and the concentration of hydrochloric acid was 31.5% by weight, with a sp. gr. of 1.16, the concentrations being recited in terms of aqueous #5 Alloys composed approximately of zinc 96%, alumi- 5 solution. num 3.8% and copper 2%. The ranges recited above relative to temperature of the TABLE 2 bath and time of immersion or treatment were successfully used and the amounts of these acids with the ranges of Formulas for Zama? #3 concentrations recited were also used successfully. The
examples recite the preferable results. Example Example Example Example Example In addition to the foregoing examples, the following 8 9 10 11 12 were also carried out successfully:
120 100 60 20 150 EXAMPLE 21 20 13.2 8 4 150 25 16 3 40 This example was the same as Example 1 but instead of 10 6.6 4 2 5 sodium fluoride, there was used ammonium fluoride. This 15 42 45 15 example illustrates the use of a compound of equivalent or greater solubility than sodium fluoride. 1 In example 11% 25 mgllitliterhs of acetitlz) acid wags sucicesfisfullilymutsed asI 51110 1 e orange SWQGD. an 111 IGI'SO narrate a EXAMPLE 22 Examples 8, 9 and 10 are solutions which may be safely This example was like Example except that it was used to produce a bright surface on Zamac #3 di a tearned out with 40 milliliters of nitric ac1d instead of 80 ings. The treatment is followed by water rinsing and a milliliters, as reclted 111 Exampl conventional bleaching dip in a dilute solution of sodium hydroxide to remove the yellow constituents in the coating EXAMPLE 23 and leave a clear bright surface as a final finish. The This example was like Example 3 except that hydrowork in this condition may be re-cleaned and then electrohlo i a id wa used instead of sulfuric acid, and the plated With other metals, for example, copper, ni k l, example was satisfactorily carried out using a lower limit Chromium. EXampl 11 i a S lution uita le f r P 0 of 3 milliliters of hydrochloric acid, an upper limit of 10 dllcing a bright Yellow fillishxwhich y be 118661 38 a final 3 milliliters of hydrochloric acid, and intermediate amounts. finish. Example 12 is a solution which contains the constituents in the proportions in which they are depleted in EXAMPLE 24 normal operation. It is intended for use in replenishing 110-180 g./1. C103 bower solutions such as Example 8 and is not itself suitable for ffi y lfgg use alone in performing the functions of this invention. 50410 mL/l. HNO
TABLE 3 Formulas for Zamac #5 Example Example Example Example Example Example Example Example 13 14 15 16 17 18 19 20 Examples 13, 14 and 15 perform the same functions for EXAMPLE 25 Zamac #5 as is performed for Za-mac #3 by Examples 8, 9 and 10, namely, chemical polishing for a clear bright final finish or in preparation 'for subsequent plating. If the sodium hydroxide or other bleaching dip is omitted, Example 15 may be used for a yellow final finish. Example 16 is a solution for maintaining the solutions ofrExamples 13, 14 and 15 in opera-ting condition and corresponds to Example 12.
Examples 17 and 18 are for applying a thin, light yellow coating on die castings with a minimum of attack on the metal and, therefore, a minimum consumption of chemicals.
Examples 19 and 20 are adapted for use with either Zamac #3 or Zamac #5.
All of the foregoing examples, namely, those as set forth in Tables 1, 2 and 3 above, were operated with the 'bath at a temperature of about 140 F. for an immersion time of about 30 seconds, except Example 20, which is formulated to operate at about 80 F. The higher concentration of the fluoride salt in this example makes this possible. The concentration of hydrofluoric acid was 60% by weight, with a sp. gr. of 1.24, the concentration of the nitric acid was 61.4% by weight, with a sp. gr. of 1.38, the sp. gr. of sulfuric acid was 93.5% by weight, with a sp.
40-90 g./l. OrOa 10-40 g./l. Nmnrg User will add:
20-50 mJ./l. HNOa Formulas 24 and 25 may be sold as a powder and the user will add the required amount of HNO EXANCPLE 26 Example 26 will be sold either-with or without the HNO The following formulation was used on Zamac #3 castings which were then given conventional electroplating coatings of copper, chromium and nickel, respective- EXAMPLE 2? 99 g./l. CrO
2s mL/l. HNO 6.6 mL/l. H SO 13.2 g./l. NH HF 42 ml./1. HAc
The dip temperature, as with the other examples recited above, was 140 F. and the immersion time was 30 seconds.
Examples or 27, preferably Example 27, is used prior to conventional electroplating with copper, chromium or nickel and the castings, both before and after electroplating, have an appearance of being hand buffed or polished, more so, however, when electroplated.
EXAMPLE 28 This formulation Was used on a Zamae #5 casting (96% zinc, 3.8% aluminum and 2% copper) to give a semi-polish or bright yellow finish:
30 g./l. CrO rnL/l. HNO 2 mL/l. H 50 4 g./l. NH HF ml./l. HAc 7.5 ml./l. HCl
Likewise, the temperature of the coating bath was 140 F. and immersion time seconds.
EXAMPLE 29 In addition to the replenishing baths referred to above, Example 8 for illustration, as well as Examples 10 and 11 and other of the examples, Was fortified or replenished, i.e., maintained, from time to time to economically increase its operating life by adding to it and preferably to the baths for Zamac castings of Examples 1 to 27, notably Examples 6, 10 and 27, the following formulations:
150 g./l. CrO 150 ml./l. HNO 5 ml./l. H 80 15 ml./l. HAc 4O g./l. NH HF The bath temperature was continuously 140 F. and the immersion time the same as described, i.e., 30 seconds. Another example of a replenishing composition useful in connection with various of the examples described above, and particularly with Examples 14 and 28, is the following:
EXAMPLE 30 150 g./l. CI'O 150 rnL/l. HNO 5 ml./l. H SO 30 ml. /l. HAc 40 g./l. NH HF 30 ml./l. HCl
This replenishing or maintaining solution added to Examples l4 and 28, which are preferably used on Zamac castings, economically improves the operating life of the solutions of these examples, the temperature of the bath and immersion time being the same as described above, namely, about 140 F. for about 30 seconds.
EXAMPLE 31 From the foregoing it will be noted that one basic formula for a bright protective finish comprises about: 120 g./l. CrO 40 g./l. NH HF 50 ml./l. HNO
The addition of HCl and H 80, act as catalysts to reduce the required fluoride. The salt spray test results, applied to all examples, were usually favorably improved by the addition of these mineral acids.
EXAMPLE 32 A formula for Zamac #5 casting is as follows:
120 g./l. C10 20 g./l. NH HF 50 ml./l. HNO 4O ml./l. HCl 10 ml./1. H 50 When HAc in amount of about 15 ml./l. is added, as in Example 13, this improved the bleaching characteristics of the film produced on the zinc castings, enabling the obtaining of a clear film. In adding the HAc, in some cases, no HCl is needed with Zamac #3 castings which do not include copper.
EXAMPLE 33 A preferred formulation for Zamac #3 castings comprises:
100 g./l. CrO 25 ml./1. HNO 30 mL/l. HAc 10 ml./l. H 40 g./l. NH HF EXAMPLE 3'45 For a Zamac #5 casting (zinc, aluminum and copper) a preferred formulation is:
g./l. CrO 60 ml./l. HNo 10 ml./l. n so, 20 g./l. NH4HF2 40 g./l. HCl
30 m1./l. HAc
With all of the formulations described herein replenishing or maintenance solutions, as described above, are used.
For the preferred formulations I find that with the CrO in varying amounts, as indicated above, about 5 to 30 ml./l. HNO 15 to 45 m1./1. HA0 5 to 10 m1./l. H 80 10 to 25 g./l. NH HF and 3 to 40 mL/l. HNO
produce useful coating and treating compositions. The CrO content is varied as indicated from about 30 g./l. upward.
In the broad range, and as explained, the concentration of the acetic acid will vary between 0 to 100 ml./l., preferably 15 to 50 ml./l.; of the nitric acid between about 4 and 80 ml./l., preferably 4 to 60 ml./ 1.; of the sulfuric acid between about 0.1 to 10 ml./l., preferably 2 to 8 ml./l.; and of the hydrochloric acid between about 0 to 50 ml./l., preferably about 3 to 40 ml./l.
Conventional bleaching with NaOH of the coatings in the various treatments described herein is unnecessary if a yellow finish is desired, and, likewise, such bleaching may be eliminated because the formulations mentioned, of themselves, produce either a clear or yellow finish, which is bright, in any case.
Where the amount of HNO is high, the use of other of the mineral and organic acids may be reduced. The same is true when the HCl is increased, i.e., reduction in the amount of such other acids is possible.
The bath temperatures succesfully used with the formulations of this application vary between F. and 160 F. but preferably F. is used. Also, I have used time periods of treatment from 5 seconds to 2 minutes with the various formulations but prefer a treatment of about 30 seconds.
While ammonium bifluoride is preferred, sodium fluoride and other fluorides of equivalent or greater solubility may be used as indicated in the foregoing examples.
Referring to Examples 12, 16, 29 and 30, and the other replenishing and maintenance solutions, these contain the same constituents as the baths they are used to maintain, and it is critical that the CrO and HNO are present in such replenishing solutions in substantial excess over the other constituents of these maintenance solutions.
I claim:
1. The process of treating zinc castings comprising immersing the same in an aqeueous acidic chromate bath containing CrO at least about 30 -g./ 1., and about 5 to 60 ml./l. I-INO 0 to 100 mL/l HAc, 2 to 10 ml./l. H SO and 4 to 50 g./l. of a soluble fluoride, for from 5 seconds "contains 3 to 40 BIL/1. HQ.
3. The process according to claim 1 wherein the temperature of the bath is between about 110 F. and 160 F.
4. The process of treating zinc castings comprising immersing the same in an aqueous acidic chromate bath con taining CrO about 60 g./l., and about 5 to 60 ml./l. HNO to 100 mL/l. HAc, 2 to 10 ml./l. H 80 and 4 to 50 *g./l. of a soluble fluoride, for from seconds to 2 minutes with the bath at a temperature between about 110 F. and 160 F.
5. The process of treating zinc castings comprising immersing the same in an aqueous acidic chromate bath containing CrO about 99 g./l., and about 5 to 60 m1./l. HNO 0 to 100 ml./l. HAc, 2 to mL/l. H 80 and 4 to 50 -g./l. of a soluble fluoride, for from 5 seconds to 2 minutes with the bath at a temperature between about 110 F. and 160 F.
6. The process of treating zinc castings comprising immersing the same in an aqueous acidic chromate bath containing CrO about 120 g./l., and about 5 to 60 ml./l. HNO 0 to 100 -m1./ l. HAc, 2 to 10 ml./-l. H 50 and 4 to 50 g./1. of a soluble fluoride, for from 5 seconds to 2 minutes with the bath at a temperature between about 110 F. and 160 F.
7. The process of treating zinc castings comprising im 8 rnersing the same in an aqueous acidic chromate bath containing CrO about 100 -g./1., and about 5 to 60 rnL/l. HNO;,, 0 to 100 ml./l. HAc, 2 to 10 mL/l. H SO and 4 to g./l. of a soluble fluoride, for from 5 seconds to 2 minutes with the bath at a temperature between about 110 F. and 160 F.
8. The process of treating zinc castings comprising immersing the same in an aqueous acidic chromate bath containing CrO at least about 30 g./l., and about 5 to ml./l. HNO 0 to mL/l. HA0, 2 to 10 mL/l. H 50 and 4 to 50 g./l. of a soluble fluoride, for from 5 seconds to 2 minutes with the bath at a temperature bet-ween about F. and 160 F. and HCl, about 3 to 40 m1./l.
9. The process of treating zinc castings comprising immersing the same in an aqueous acidic chromate bath containing CrO about g./l., and about 40 mL/l HNO' about 15 ml./l. HAc, about 10 ml./l. H 50 about 10 mL/l. HCl and about 30 g./l. NH HF for from 5 seconds to 2 minutes with the bath at a temperature of about 80 F.
References Cited in the file of this patent UNITED STATES PATENTS 2,186,579 Dubpernell Jan. 9, 1940 2,613,165 Fischer Oct. 7, 1952 2,614,913 Reindl et al Oct. 21, 1952 2,796,372 Chester June 18, 1957 2,904,413 Hampel Sept. 15, 1959 2,955,027 Newell et a1. Oct. 4, 1960

Claims (1)

1. THE PROCESS OF TREATING ZINC CASTINGS COMPRISING IMMERSING THE SAME IN AN AQUEOUS ACIDIC CHROMATE BATH CONTAINING CRO3, AT LEAST ABOUT 30G./1., AND ABOUT 5 TO 60 ML./1. HNO3, 0 TO 100 ML./1 HAC, 2 TO 10 ML./1. H2SO4 AND 4 TO 50G./1. OF A SOLUBLE FLUORIDE, FOR FROM 5 SECONDS TO 2 MINUTES WITH THE BATH AT A TEMPERATURE BETWEENEEN 80*F. AND 160*F.
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Cited By (2)

* Cited by examiner, † Cited by third party
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US3232802A (en) * 1963-03-11 1966-02-01 North American Aviation Inc Process of etching and etching bath for nickel base alloys
US4215005A (en) * 1978-01-30 1980-07-29 Allied Chemical Corporation Organic stripping compositions and method for using same

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US2186579A (en) * 1933-06-28 1940-01-09 Udylite Corp Method of brightening metals electronegative to iron
US2613165A (en) * 1950-07-03 1952-10-07 Aluminum Co Of America Surface treatment of magnesium and magnesium alloy articles
US2614913A (en) * 1950-10-20 1952-10-21 Gen Motors Corp Brightening bath
US2796372A (en) * 1953-05-07 1957-06-18 Poor & Co Corrosion protecting metal finishing composition
US2904413A (en) * 1954-06-23 1959-09-15 Jervis Corp Process of bright dipping zinc base alloys
US2955027A (en) * 1957-08-07 1960-10-04 Isaac L Newell Method for the deburring of zinc-base die castings

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2186579A (en) * 1933-06-28 1940-01-09 Udylite Corp Method of brightening metals electronegative to iron
US2613165A (en) * 1950-07-03 1952-10-07 Aluminum Co Of America Surface treatment of magnesium and magnesium alloy articles
US2614913A (en) * 1950-10-20 1952-10-21 Gen Motors Corp Brightening bath
US2796372A (en) * 1953-05-07 1957-06-18 Poor & Co Corrosion protecting metal finishing composition
US2904413A (en) * 1954-06-23 1959-09-15 Jervis Corp Process of bright dipping zinc base alloys
US2955027A (en) * 1957-08-07 1960-10-04 Isaac L Newell Method for the deburring of zinc-base die castings

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3232802A (en) * 1963-03-11 1966-02-01 North American Aviation Inc Process of etching and etching bath for nickel base alloys
US4215005A (en) * 1978-01-30 1980-07-29 Allied Chemical Corporation Organic stripping compositions and method for using same

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