US2813814A - Composition and process for forming phosphate coatings on titanium and zirconium - Google Patents

Composition and process for forming phosphate coatings on titanium and zirconium Download PDF

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US2813814A
US2813814A US448121A US44812154A US2813814A US 2813814 A US2813814 A US 2813814A US 448121 A US448121 A US 448121A US 44812154 A US44812154 A US 44812154A US 2813814 A US2813814 A US 2813814A
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titanium
zirconium
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bath
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Edwin W Goodspeed
Frank G Pollard
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Parker Rust Proof Co
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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
    • C23C22/36Chemical 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 phosphates
    • C23C22/364Chemical 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 phosphates containing also manganese cations
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B21MECHANICAL METAL-WORKING WITHOUT ESSENTIALLY REMOVING MATERIAL; PUNCHING METAL
    • B21CMANUFACTURE OF METAL SHEETS, WIRE, RODS, TUBES OR PROFILES, OTHERWISE THAN BY ROLLING; AUXILIARY OPERATIONS USED IN CONNECTION WITH METAL-WORKING WITHOUT ESSENTIALLY REMOVING MATERIAL
    • B21C37/00Manufacture of metal sheets, bars, wire, tubes or like semi-manufactured products, not otherwise provided for; Manufacture of tubes of special shape

Description

United States Patent fifice 2,813,814 Patented Nov. 19, 1957 COMPOSITION AND PROCESS FOR FORMING PHOSPHATE COATINGS ON TITANIUM AND ZIRCONIUM Edwin W. Goodspeed, Royal Oak, and Frank G. Pollard,
Ferndale, Mich., assiguors to Parker Rust Proof Company, Detroit, Micln, a corporation of Michigan No Drawing. Application August 5, 1954, Serial No. 448,121
16 Claims. (Cl. 1486.15)
The present invention relates generally to adherent, protective coatings on titanium and zirconium metals. More specifically, the invention relates to the application of phosphate coatings on elementary titanium and zirconium and their alloys.
In recent years, the supply of titanium metal has been greatly increased by improvement in techniques of refinement. The extremely valuable properties of this metal have led to its use in a great variety of applications, in which the metal is worked, drawn, and otherwise stretched and shaped. Likewise, while not yet in plentiful supply, zirconium metal and its alloys have been found to have extremely valuable properties. As with other metals, an adherent, protective coating has been sought to facilirate the working of these metals and also to protect the metals themselves. type treating baths do not produce entirely satisfactory coatings on titanium or zirconium. With these solutions either the metal is not coated at all, or there is formed only a loose, dusty coating which is unsatisfactory in the drawing operation.
It has been found, in accordance with this invention, that titanium and zirconium may be provided with uniform, hard and adherent phosphate coatings by contacting a surface of the metal with a bath comprising an aqueous solution of manganese dihydrogen phosphate, the fluoride ion, and a small amount of a stable oxidizing agent. While good coatings are obtained in the treating baths of this invention which contain no dissolved titanium or zirconium it has been found that the general quality of the coatings obtained under conditions of industrial application is improved, and more consistent operation is insured, if a very small proportion of titanium or zirconium is added to the bath at the start. The titanium or zirconium content for this purpose may be derived from a soluble salt such as titanyl sulfate TiOSO4 potassium fluotitanate (KzTiFs) and soluble zirconium compounds or the bath may be aged in the presence of metallic titanium or zirconium until the necessary amount is dissolved. Improved coating action and more consistent operation is noticeable when the concentration of Ti or zirconium in the bath is at least about .05% by weight. The effect of titanium ion on the coating action of the solution on zirconium is not as great as that of zirconium ion. The effect of zirconium ion on the coating of titanium likewise is less than that of the titanium ion. For these reasons, it is preferred that the titanium ion be present when coating titanium and the zirconium ion be present when coating zirconium.
Under ordinary production conditions of repeated or continuous use, the free titanium or zirconium ion content of a treating bath slowly builds up and as this occurs, the coating efficiency of the bath is gradually impaired. We have found, however, that full efficiency of such a bath is restored and easily maintained by periodic additions of fluoride ion. Thus, the treating baths of this invention are well adapted to commercial coating operations on a continuous scale.
Conventional phosphate and oxalate- While in no wise necessary for obtaining coatings of satisfactory weight and adherency, it has been found that improved coatings and more satisfactory and reliable operation of the treating bath are obtained if there is present an ion such as ammonium, or a combination of ammonium with sodium, potassium and the like; or a combination of sodium and potassium ions, with or without ammonium ion. Thus, while the effect of the ammonium ion is always beneficial, the presence of either sodium or potassium ions, alone, seems to be without effect. In contrast, a combination of sodium and potassium ions seems to improve the action of the bath in a manner similar to that of the ammonium ion. To derive this beneficial effect only a small proportion of ammonium and/ or sodium plus potassium ions are required. In general, only 0.02% of ammonium ion or its equivalent in sodium and potassium is required. Better results are obtained with 0.03 to 0.04%. While not deleterious, no further significant improvement is noted with more than 0.2% ammonium ion or its equivalent of sodium plus potassium ions.
While phosphate solutions, other than those of manganese phosphate, will produce coatings on titanium or zirconium, such coatings are not entirely uniform or otherwise satisfactory. For example, zinc phosphate coatings do not improve drawing or other working operations to nearly the same extent as do manganese phosphate coatings. Solutions in which manganese dihydrogen phosphate is the major or predominating coating constituent, however, produce harder, more tightly adherent, and heavier coatings on a wider variety of titanium and zirconium metals and their alloys. Moreover, the coatings derived from manganese phosphate solutions are of greatly superior quality in metal working operations. The proportions of manganese dihydrogen phosphate in the coating solution of this invention are in no wise critical. For example, excellent, hard and tightly adherent coatings are obtained in solutions containing from as little as 0.5% to as much as saturation. A typical bath for use in this invention will contain from 2 to 10% manganese dihydrogen phosphate. The effectiveness of the bath increases with increases in manganese phosphate content in the range between 3 and 9%. The phosphate solution may vary considerably in its free acid" and total acid" content. (The former is the number of ml. of N/l0 sodium hydroxide solution required to neutralize 2 ml. of the phosphate solution to a bromophenol blue end-point while the latter is the number of mi. of N/lO sodium hydroxide solution required to neutralize 2 ml. of solution to a phenolphthalein end-point.) With typical solutions, excellent coatings are obtained when the ratio of free acid to total acid is in the range 1:4 to 1:7. Stable, concentrated stock solutions may be prepared containing at least twice the useful concentration of manganese dihydrogen phosphate and other ingredients disclosed below, these solutions merely being diluted with water before use or added to an existing bath as a replenisher.
The concentration of oxidizing agent does not appear to be critical providing sumcient is utilized to insure coating action. With as little as 0.7% sodium nitrate (equivalent to about 0.5% nitrate ion), a preferred oxidant in this composition, excellent, uniform and adherent coatings are obtained. It is preferred, however, to use somewhat larger quantities to insure a slight excess of oxidant. In commercial treating baths containing from 2 to 10% manganese dihydrogen phosphate, it is preferred to utilize about 1.5 to 1.75% sodium nitrate or its equivalent. Concentrations up to saturation may be satisfactorily employed. Other oxidizing agents which are somewhat weaker than potassium permanganate or potassium persulfate. for example, may be satisfactorily employed, such as for example ammonium nitrate, sodium chlorate. sodium nitrite. saccnarin, sucrose and others. Saccharin in amounts between 0.2 and has been found to yield uniform adherent coatings. With sucrose only about 0.2 to 2% is required for similarly good coat ings. Sodium nitrite. which decomposes in acid solution at elevated temperatures. pr duces uniform adherent coatings it added lowhv and culniniiotr-ly iii a rate to maintain a concentration of abruit 0.0V)! nliinn cblo ratc in amounts between 0.7 and 3.5% elfcctively inc proves coating action. In any case, irrespective of the particular oxidizing agents utilized, the oxidizing agent should be utilized in quantities equivalent in their effect on the coating action of the solution to about 0.7% or more sodium nitrate.
The concentration of the free fluoride ion is not critical providing there is a small amount present which is not complexed with titanium. zirconium or other polyvalent metals in the solution. Solutions which are saturated with fluoride ion have produced adherent coatings on titanium and zirconium metals. As little as 0.030 seems to be sufficicnt in solutions very low in titanium and zirconium. Heavier. more adherent coatings are obtained when at least 0.2% fluoride ion is present. It has been found that the actual amount of fluoride ion present in the bath is not determinative of the quality. weight or adherence of the coatings obtained, but rather it has been found that heavy. adherent and high-quality coatings are obtained whenever there is present free fluoride in slight excess over that theoretically required to form TiFs ion or other complex with the titanium or zirconium content of the bath. ln a bath containing about 8% manganese dihydrogen phosphate dihydrate. heavy, adherent. and highquality coatings are obtained on titanium or zirconium when the fluoride ion is present in an excess at least 0.09% over that theoretically required to form TlFG ion or a zirconium complex with the titanium or zirconium dissolved in the bath. In order to avoid frequent rc-- plenishing of the fluoride content of the bath during use. it is usually desirable to have a considerable excess of fluoride ion present. For this latter purpose 0.15 to 2.5% free fluoride ion usually is sufl icient.
The fluoride content of the bath may be derived from any water-soluble fluoride or bifluoride such as the alkalimetal and ammonium fluorides and bifiuorides. Ammonium bifiuoride (NI-14111 2) sodium bifluoride and potassium bifluoride are much preferred. because they also function as a source of the desirable ammonium, sodium and potassium ions.
In the method of this invention, processing temperatures between about 190 F. and boiling may be used satisfactorily. As the temperature is increased above about 190 F.. the time required for coating is decreased. For example. at a temperature of about 195 F., a satisfactorily adherent coating is obtained in minutes. At temperatures of 200 F.. or more. satisfactory coatings are obtained in about 15 minutes.
No special pretreatment of the titanium or zirconium metals is required before applying the coating. Generally, however. it is desirable to subject the metal to the nitric acidhydrofluoric acid activation pretreatment conventionally employed in connection with stainless steels, followed by a hot water rinse. Any grease, oil, or soil may be removed by wiping. spraying, or dipping in mineral spirits or other solvents, or by use of an alkali cleaner, preliminary to the nitric acid-hydrofluoric acid pretreatment.
The coatings applied by the method and compositions of this invention provide added protection to the metal against corrosion. When the coatings are to be used as a base for paint. it is desirable to follow the coating formation step with the conventional chromic acid rinsing step. When the coated titanium or zirconium is deformed, it is advantageous to follow the phosphate coating step with t application of conventional drawing lubricants 4 such as stearate soaps prior to the actual deformation operation.
By the term titanium metal" or zirconium metal" as used herein, is meant any of the commercially-available forms of titanium or zirconium and any alloys thereof in which ti anium or rirco ium is prc ent in a greater quantity than that of an otlnr Illxllti and preferably in a preponderuting proportion. 'lilaninni and i'irconiuln alloy readily with mail all metals. including especially copper. tin. iron. aluminum, chromium. cobalt. molybdenum and tungsten. Titanium, zirconium and alloys thereof. or of either with the above and other metals, particularly the commercial varieties thereof. may be worked by swaging. hot and cold rolling and wire drawing. Titanium metal. in particular. oxidizes and reacts with nitrogen vcry readily when hot. Consequently. an adherent. protective coating is of great value during the working of this metal. especially during wire drawing. The coating in conjunction with lubricants makes pos sible higher drawing speeds. "rcatcr reduction per draw and higher finish.
The invention will now be more fully described with reference to several specific examples. As used hereinabove and unless otherwise specified, the concentrations or" the various ingredients are expressed as percent wt./vol. In. other words. the density of the solution is taken as unity.
EXAMPLE 1 The following materials were added to sutllcient water to make a total volume of 600 ml.:
lcrccnt effective agcnt--.v./ vol.
Mn(H2PO-i)2.2H2O 25.5 grams-4.2% NaNOa 2 4 grams-0.7%
N HtH F: o grams-A .0 r'
A panel of commercially pure titanium was immersed in this bath for l5 minutes while maintaining the tcrnpcr attire at 200 F. An excellent practical coating was ol1- tained. On continued use of the bath. it was necessary to replenish the fluoride ion by small increments of NHqHFQ. Full bath activity is easily n ruined, on con tinuous or extended use. by periodic replenishing wYth the other ingredients.
EXAMPLE 2 A concentrated stock solution was prepared containing the following ingredients:
h'lntHziOUzlHzO grarns 2.0410 NaNOz 340 NHiHFz l70 Water ml 6,000
The final volume was 7.000 ml. This solution was stored for a moderate period with only slow precipitation. This stock solution may be diluted with water un til the resulting solution contains about 8% manganese dihydrogen phosphate and used to provide excellent coatings on titanium as in Example 1.
EXAM P l. E 3
To demonstrate the operation of the process in a con-- tinuous manner, a large gallon bath nus made up for intermitten commercial scale use as follows:
l h-.. Mn(H2PO-1)2.2H2O ll2 NHtHF2 2 0 NaNOs 2 H20 to total 150 gals.
The bath continued to produce uniform, adherent coatings on titanium over the course of many months. From time to time small additional quantities of NHtHFz were added to maintain the desired fluoride level. Had a greater volume of metal been processed replenishment of the other ingredients would have been required. The bath amply demonstrated that it was stable over long periods.
EXAMPLE 4 The effect of ammonium ion was effectively demonstrated by the use of the following bath:
Grams Mn(H2PO4)2.2H2O 125 NaHFz 10 NaNOa 10 H2O to 1,500 ml.
Panels of commercially pure titanium processed 70 minutes at 200210 F. in this solution received almost no coating. At this point, the solution analyzed as having F. A.4.5; T. A.18.5; ratio 1:4.1. When only grams of (NH4)2HPO4 were added to this solution a subsequent panel received an excellent, heavy, hard and adherent coating in 15 minutes at 200-210" F.
EXAMPLE 5 A bath was made up to have the following composition:
Percent w./vol. M11(H2PO4)2.2H2O 8.3 NaNOs 0.67 NH4HF2 0.67
This bath was heated to 200 F. and maintained at 200 F.-210 F. for 2 to 3 hours. A tube of commercially pure zirconium was pretreated in HNO3HF, rinsed in hot water, immersed for 15 minutes in the bath at 200 F., rinsed again in hot water and dried. The tube received a thin coating by this treatment. At this point the analysis of this bath was free acid2.8 ml., total acid12.6 ml., ratio F. A.:T. A.1:4.5. Further processing of the same tube resulted in considerable improvernent in the coatings. The finally coated zirconium tube was lubricated with stearate soap and subjected to drawing. Drawing Operations were found to be definitely improved over the drawing of uncoated zirconium.
From the above it is clear that the presence of zirconium ion in the bath improves the coating action of the solution on zirconium to a noticeable extent. When zirconium panels are processed in a similar bath which had been used to coat titanium, a heavy, uniform coating was obtained which was not as adherent as those prepared in the presence of zirconium ion.
EXAMPLE 6 The efiiciency in metal drawing of zinc phosphate coated titanium was compared to that of manganese phosphate coated titanium. The zinc phosphate solution and procedure utilized were as follows:
Weightgrams ZI1(H2PO4)2.2H2O 13.1 NaClOg 3.6 NHdHFz 4.0 Sodium salt of ethylene-diamine tetraacetic acid--- 1.0 H20 to 600 ml.
Processing time-l5 minutes.
Processing temp.120l 50 F.
The above procedure formed a phosphate coating on tubes of commercially pure titanium. A manganese phosphate coated tube, prepared according to the procedure of Examples 1 to 3 was utilized in the compari son. Both tubes were lubricated with sodium stearate before drawing. The zinc phosphate coated tube did not draw as satisfactorily as the tube coated with manganese phosphate. The latter is suitable for commercial drawing operations while the former is not.
6 EXAMPLE 1 For commercial coating of titanium a two package composition was developed, one solution for original make-up and the other a concentrated replenisher solution for replenishing a hath made from the make-up solution. The materials of the two solutions were mixed in the following proportions:
Make-up Weight-grams Mn(H2PO4)2.2H2O 80.00 HNOs (42 Baum) 3.00 NaNOs 10.90 NaHFz 0.90 KzTiFe 2.10 Water 94.9
Total 191.8
(133 ml. vol.)
Replenisher Mn(H2PO4)2.2HzO 80.00 Nitric acid (42 Baum) 7.70 KNOa 3.70 Water 94.80
Total 186.2
(135 ml. vol.)
In the above formulations the nitric acid or other mineral acid was added to keep the ingredients in solution. Before use, the acidity of the make-up was reduced to a desired value by adding a small amount of manganese carbonate. The acid content of the replenisher as given above is such as to maintain correct acidity in the made-up bath throughout its period of use. Since sodium bifiuoride is of limited solubility when cold, a sufiicient amount cannot be incorporated in either of the make-up or replenisher solutions. This ingredient must be added periodically by itself. The above proportion of bifluoride, however, is stable on storage, lesser or greater amounts seemingly favoring the formation of a precipitate. The makeup contains both sodium and potassium ions and also titanium ions. The replenisher contains potassium ions in sufficient concentration to combine with the sodium bifluoride additions to maintain a satisfactory sodiumpotassium level and obtain the above-discussed accelerating and improvement action.
In use the make-up solution is first diluted with water, each lb. portion of make-up being diluted with sufficient water to make 100 gals of solution. The diluted solution is then heated in ZOO-210 F. and 1.7 lbs. of manganese carbonate is added to reduce the acidity. Two pounds (2 lbs.) of sodium bifiuoride are finally added and the bath is ready for use.
As the bath is utilized the total acidity will gradually decline due to depletion. The addition of 10 pounds of replenisher for every 100 gals. of the bath will raise the total acidity of the make-up solution by one point. On continued use small portions of sodium bifluoride are added as needed to maintain the free fluoride level and bath activity. The above formulas produce consistent, excellent coatings on commercially-pure titanium metal. The formulas can be varied in strength and in proportion, it being understood that the solutions should be dilutable to produce final solutions having concentrations within the ranges of proportions given herein.
EXAMPLE 8 A second type of concentrated make-up and replenisher solutions, which employ the ammonium ion as an acceldid not in any way affect the utility of the solution.
erator in place of the sodium-potassium combinations of Example 7. was made up as follows:
The treating bath was made by diluting the make-up solution as in Example 7. The replenisher solution was used periodically to restore full bath strength. Sodium bifluoride also was added periodically to maintain an excess over the titanium or zirconium in the bath. The bath 01' this example was slightly superior in coating efficiency to that of Example 7.
EXAMPLE 9 A single concentrated solution which is useful both as a make-up and as a replenisher solution was made up as follows:
This stock solution was made by mixing the acid and water and then adding the solid chemicals thereto. The solution was stirred for about 1.5 hours and then filtered. After 27 days storage in glass bottles at room tempera ture, only a slight, light-Weight precipitate formed which For analysis. 60 grams of the above solution was diluted to 1000 ml. with distilled water and 10 ml. aliquots of the resulting solution analyzed for free acid and total acid using bromophenol blue and phenolphthalein indicators. respectively. The free acid of the solution was 3.03 ml.. the total acid 23.17 ml. and the specific gravity at 85 C. was 1.365.
The treating bath was made up by adding 175 lbs. of the above solution to enough water to make 100 gallons. The solution was then heated to 200210 F. and 4.3 lbs. manganese carbonate, 1.8 lbs. of KzTiFs, and 2.85 lbs. of NHHFQ added for every 100 gallons of solution. Commercially pure titanium. pretreated for one minute at room temperature in a solution containing 3% HF and 10% HNOs, processed for 15 minutes in the resulting bath acquired uniform, excellent coatings weighing an average of about l04 mgJft.
EXAMPLE 10 Other oxidizing agents useful as replacement for sodium nitrate were added to a bath containing about 8.3% manganese dihydrogen phosphate, about 0.7% am monium bifluoride. and about 0.1% titanium ion. Baths containing from 0.2 to 20% of saccharin. 0.7 to 2.5% sodium chlorate, or 0.2 to 2% sucrose yielded uniform adherent coatings at ZOO-210 F. A dilute solution of sodium nitrite was slowly trickled into a similar bath at a rate to maintain a concentration estimated to be of the order of 0.01%. With this bath, satisfactory coatings on titanium also were obtained.
While there have been disclosed certain preferred Ways of carrying out the invention, it is desired not to be limited solely thereto, and it will be appreciated that the invention is susceptible to modification, variation and change without departing from the proper scope or fair meaning of the subioined claims.
lit)
What is claimed is:
1. The process of producing an adherent, protective coating on a surface of titanium and zirconium metals which comprises contacting a metal surface with an aqueous solution consisting essentially of manganese dihydrogen phosphate. at least about 0.05% by weight of at least one ion selected from the group consisting of titanium inns and zirconium ions. an oxidizing agent in an amount having an cll'ect on the coating-forming ability of said solution equivalent to about 0.5% to about 1.3% of the nitrate ion and the fluoride ion in an amount in excess of the concentration of the ion selected from the group consisting of titanium and zirconium ions.
2. The process of treating a surface of titanium and zirconium metals to produce an adherent, protective coating thereon, which process comprises contacting said surface with a solution consisting essentially of manganese dihydrogen phosphate, at least about 0.05% by weight of at least one ion selected from the group consisting of titanium and zirconium ions, an oxidizing agent in an amount having an effect on the coatingforming ability of said solution equivalent to about 0.5% to about 1.3% nitrate ion, about 0.02% to about 0.2% of at least one ion selected from the group consisting of ammonium, sodium and potassium ions, and the fluoride ion in an amount in excess of the concentration of the ion selected from the group consisting of titanium and zirconium ions.
3. A process of producing an adherent, phosphate coating on the surface of titanium and zirconium metals, which process comprises contacting a surface of said metal with an aqueous solution comprising manganese dihydrogen phosphate, fluoride ion, ammonium ion, a metal ion selected from the class consisting of titanium and zirconium, and saccharin; wherein the fluoride ion is in excess of said metal ion, said ammonium ion is present to the extent of at least 0.02%. said metal ion is present to the extent of at least about 0.05%, and said saccharin is present in amounts between 0.2 and 20%.
4. A composition for the phosphate coating of titanium and zirconium metals which comprises an aqueous solu tion of a coating phosphate comprising predominantly manganese dihydrogen phosphate, a stable oxidizing agent in an amount having an effect on the coatingforming ability of said solution equivalent to about 0.5% to about 1.3% of the nitrate ion, at least about 0.05% by weight of at least one ion selected from the group consisting of titanium and zirconium ions, and the fluoride ion in an amount in excess of the concentration of the ion selected from the group consisting of titanium and zirconium ions.
5. A composition for producing an adherent, phosphate coating on titanium and zirconium metals which consists essentially of an aqueous solution of manganese dihydrogen phosphate, at least about 0.05% by weight of at least one ion selected from the group consisting of titanium and zirconium ions. an oxidizing agent in an amount having an effect on the coating-forming ability of said solution equivalent to about 0.5% to about 1.3% nitrate ion, about 0.02% to about 0.2% of at least one ion selected from the group consisting of ammonium. sodium and potassium ions, and the fluoride ion in an amount in excess of the concentration of the ion selected from the group consisting of titanium and zirconium ions.
6. A process in accordance with claim 1 wherein the said surface is titanium and the fluoride ion is present in an excess of at least about 0.09% over that which is requircd to form a titanium ion complex with the titanium ions in said solution.
7. A process in accordance with claim 1 wherein said surface is zirconium and the fluoride ion is present in an excess of at least about 0.09% over that which is required to form a zirconium ion complex with the Zirconium ions which are present in the solution.
8. A process in accordance with claim 1 wherein said oxidizing agent is selected from the group consisting of about 0.5 to about 1.3% nitrate, about 0.5 to about 1.9% chlorate, about 0.01% nitrite, about 0.2% to about 20% saccharin and about 0.2 to about 2% sucrose.
9. A composition in accordance with claim 4 wherein the said fluoride ion is present in an amount in excess of at least about 0.09% over that which is required to form a titanium ion complex with the titanium ions in said solution.
10. A composition in accordance with claim 4 wherein the said fluoride ion is present in an amount in an excess of at least about 0.09% over that which is required to form a zirconium ion complex with the zirconium ions in said solution.
11. A process in accordance with claim 1 wherein said oxidizing agent is selected from the group consisting of about 0.5 to about 1.3% nitrate, about 0.5 to about 1.9% chlorate, about 0.01% nitrite, about 0.2% to about 20% saccharin and about 0.2 to about 2% sucrose.
12. A process in accordance with claim 8 wherein said oxidizing agent is nitrate.
13. A composition in accordance with claim 11 wherein said oxidizing agent is nitrate.
14. An article of manufacture having a surface at least of a metal selected from the class consisting of titanium, zirconium, and alloys thereof and an adherent manganese phosphate coating on said surface derived from an aqueous acidic solution comprising manganese dihydrogen phosphate.
15. An article of manufacture as claimed in claim 14 and further characterized in that said surface is a titanium metal.
16. An article of manufacture as claimed in claim 4 and further characterized in that said surface is a zirconium metal.
References Cited in the file of this patent UNITED STATES PATENTS 1,949,090 Tanner et a1 Feb. 27, 1934 2,120,212 Curtin June 7, 1938 2,234,206 Thompson Mar. 11, 1941 2,487,137 Hoover et al. Nov. 8, 1949 FOREIGN PATENTS 885,638 Germany Aug. 6, 1953

Claims (1)

1. THE PROCESS OF PRODUCING AN ADHERENT, PROTECTIVE COATING ON A SURFACE OF TITANIUM AND ZIRCONIUM METALSS WHICH COMPRISES CONTACTING A METAL SURFACE WITH AN AQUEOUS SOLUTION CONSISTING ESENTIALLY OF MANGANESE DIHYDROGEN PHOSPHATE, AT LEAST ABOUT 0.05% BY WEIGHT OF ATT LEAST ONE ION SELECTED FROM THE GROUP CONSISTING OF TITANIUM IONS AND ZIRCONIUM IONS, AN OXIDIZING AGENT IN AN AMOUNT HAVING AN EFFECT ON THE COATING-FORMING ABILITY OF SAID SOLUTION EQUIVALENT TO ABOUT 0.5% TO ABOUT 1.3% OF THE NITRATE ION AND THE FLUORIDE IN AN AMOUNT IN EXCESS OF THE CONCENTRATION OF THE ION SELECTED FROM THE GROUP CONSISTING OF TITANIUM AND ZIRCONIUM IONS.
US448121A 1954-08-05 1954-08-05 Composition and process for forming phosphate coatings on titanium and zirconium Expired - Lifetime US2813814A (en)

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US448121A US2813814A (en) 1954-08-05 1954-08-05 Composition and process for forming phosphate coatings on titanium and zirconium
DEM27838A DE1088311B (en) 1954-08-05 1955-07-29 Process for the production of firmly adhering protective coatings on surfaces made of titanium, zirconium or their alloys
FR1136307D FR1136307A (en) 1954-08-05 1955-08-03 Method and composition for forming phosphate coatings on titanium and zirconium
GB22665/55A GB780230A (en) 1954-08-05 1955-08-05 Improvements relating to the formation of chemical coatings on metal surfaces

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US4017334A (en) * 1973-10-04 1977-04-12 Oxy Metal Industries Corporation Process for treating aluminum cans
US4148670A (en) * 1976-04-05 1979-04-10 Amchem Products, Inc. Coating solution for metal surface
CN106835098A (en) * 2016-12-01 2017-06-13 三达奥克化学股份有限公司 Environmentally friendly vitrification inorganic agent and production method before iron and steel parts electrophoretic painting
CN111850534A (en) * 2020-06-16 2020-10-30 中国石油天然气集团有限公司 Martensite stainless steel oil pipe low-stress pre-passivation film and preparation method thereof

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CN1125196C (en) * 1999-09-28 2003-10-22 香港生产力促进局 Surface activating process of Ti and Ti alloy for bright electroplating

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US1949090A (en) * 1930-11-17 1934-02-27 Metal Finishing Res Corp Method and material for coating and cleaning metal
US2120212A (en) * 1936-01-10 1938-06-07 Curtin Howe Corp Phosphated metal coating
US2234206A (en) * 1935-06-03 1941-03-11 Metal Finishing Res Corp Coated aluminum
US2487137A (en) * 1947-09-10 1949-11-08 Armco Steel Corp Producing coatings on metal
DE885638C (en) * 1945-02-27 1953-08-06 Metallgesellschaft Ag Process for the production of a pre-wash solution for phosphating

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GB655079A (en) * 1946-09-11 1951-07-11 Pyrene Co Ltd Improvements in or relating to the production of phosphate coatings

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US1949090A (en) * 1930-11-17 1934-02-27 Metal Finishing Res Corp Method and material for coating and cleaning metal
US2234206A (en) * 1935-06-03 1941-03-11 Metal Finishing Res Corp Coated aluminum
US2120212A (en) * 1936-01-10 1938-06-07 Curtin Howe Corp Phosphated metal coating
DE885638C (en) * 1945-02-27 1953-08-06 Metallgesellschaft Ag Process for the production of a pre-wash solution for phosphating
US2487137A (en) * 1947-09-10 1949-11-08 Armco Steel Corp Producing coatings on metal

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4017334A (en) * 1973-10-04 1977-04-12 Oxy Metal Industries Corporation Process for treating aluminum cans
US4148670A (en) * 1976-04-05 1979-04-10 Amchem Products, Inc. Coating solution for metal surface
CN106835098A (en) * 2016-12-01 2017-06-13 三达奥克化学股份有限公司 Environmentally friendly vitrification inorganic agent and production method before iron and steel parts electrophoretic painting
CN111850534A (en) * 2020-06-16 2020-10-30 中国石油天然气集团有限公司 Martensite stainless steel oil pipe low-stress pre-passivation film and preparation method thereof
CN111850534B (en) * 2020-06-16 2022-03-01 中国石油天然气集团有限公司 Martensite stainless steel oil pipe low-stress pre-passivation film and preparation method thereof

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FR1136307A (en) 1957-05-13
DE1088311B (en) 1960-09-01
GB780230A (en) 1957-07-31

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