CA2150545A1

CA2150545A1 - Substantially nickel-free phosphate conversion coating composition and process

Info

Publication number: CA2150545A1
Application number: CA002150545A
Authority: CA
Inventors: Robert W. Miller; Michael Petschel
Original assignee: Individual
Current assignee: Henkel Corp
Priority date: 1992-12-22
Filing date: 1993-12-15
Publication date: 1994-07-07
Also published as: CZ164995A3; PL309404A1; AU5848194A; ZA939636B; ATE183247T1; EP0675972A1; DE69326021D1; SG55084A1; CN1092245C; JPH08504890A; ES2136726T3; EP0675972A4; WO1994014999A1; CZ287997B6; CN1090606A; EP0675972B1; BR9307702A; DE69326021T2

Abstract

The nickel in conventional low zinc and nickel containing phosphate conversion coating compositions can be replaced by substantially smaller concentrations of cupric ions without losing the benefits of quality that motivated the addition of nickel to low zinc phosphating compositions originally; in fact, better alkaline resistance and paint adhesion can be achieved, along with a substantial cost reduction.

Description

~o 94/14999 ~15 0 S ~ S PCT/US93/12044 Description SUBSTANTIALLY NICKEL-FREE PHOSPHATE CONVERSION COATING
COMPOSITION AND PROCESS

BACKGROUND OF THE INVENTION
Field of the Invention This invention relates to a composition and process for forming a phosphate conversion coating on active metal surfaces in order to increase the corrosion resist-5 ance of the s~ ces, either as treated or after subsequent conventional overcoating ofthe conversion coating layer formed by an organic based protective coating such as a paint or lacquer. A composition according to this invention is well adapted to treat-ing any of a variety of base metals, including at least steel and galvanized steel and ~l~lminllm and ~lnminllm based alloys.
10 Statement of Related Art A wide variety of phosph~te. conversion coating compositions and processes are already described in the art. Those believed to be generally considered of highest quality at present include zinc, nickel, and at least one other divalent metal such as m~ng~nPse in the composition.
DESCRIPrION OF THE INVENTION
In this description, except in the working ex~mples and claims and wherever expressly in~ic~t~.d to the contrary, all mlme.ric~l specifications of amounts of materials or conditions of reaction or use are to be understood as modified by the term "about" in describing the broadest scope of the invention. Practice of the invention 20 within the numerical limits given is generally preferred.
Object of the Invention Nickel has been implicated as a carcinogen in some studies, so that avoidance of its use in metal fini~hing is desirable for health reasons. Nickel is also considered a serious pollutant, and at the levels of 0.5 - 1.5 grams per liter (hereinafter often ab-25 breviated "g/L") at which it is conventionally used, nickel contributes significantly tothe cost of the zinc phosphate conve,~ion coating compositions. It is an object of this invention to minimi7~. or elimin~te the use of nickel, without wol~elling the quality wo 94/14999 PCT/US93/12044~

2 ~ 5 of conversion coating obtained with conventional compositions cont~ining zinc, nickel, and m~ng~n~se.
Summarv of the Invention A working composition according to this invention is an aqueous liquid compo-5 sition that compri.~çs, preferably consists essentially of, still more preferably consists of, water and:
(A) from 3 to 50, more preferably from 5 - 20, still more preferably from 13 - 18 g/L of dissolved phosphate ions;
(B) from 0.2 to 3, or with increasing p,ere~nce in the order given, from 0.45 to o 2.0, 0.57 to 1.24, 0.60 to 0.95, or 0.71 to 0.87, g/L of dissolved Zn+2 ions;
(C) from 1 to 200, or with increasing preference in the order given, from 20 to100, 24 to 74, or 24 to 60 milligrams per liter ("mg/L") of dissolved Cu~2 ions;(D) an effective amount of a convèntional accelerator exclusive of nitrate ions;
(E) from S to 40, or with increasing preference in the order given, from 7 to 25, 13 to 24, 16 to 22, or 18 to 21 "points" of total acid; and (F) from -1.0 to +3.0, or with increasing p~re,ence in the order given, from -0.5 to +1.5 or -0.5 to +1.0 points of free acid; for substrates other than ~ minum and operating temperatures above 40 C, ranges of 0.0 to 0.8, or better, 0.35 to 0.65 points of free acid are still more preferable; but if operation is at a temperature lower than 40 C or the substrate is ~lnminllm, ranges of -0.5 to 0.0, or better, -0.5 to -0.2, points of free acid are still more preferable; and, op-tionally, (G) up to 2 g/L, preferably from 0.1 to 0.8 g/L, or still more preferably from 0.40 to 0.65 glL of a total of Mn+2 and Co+2 ions;
(H) up to 2 g/L, preferably from 0.5 to 1.0, or still more preferably from 0.70 to 0.80 g/L of Mg+2 ions; and, optionally, (J) up to 5.5, preferably 1.0 to 4.0, still more preferably from 1.5 to 2.5, g/L of free fluoride as measured by a fluoride sensitive electrode; and, optionally, (K) not more than 40, or, with increasing p,erelellce in the order given, not more than 20 or 11 g/L of So4-2 ions; and, optionally, (L) not more than 4.5, or, with increasing preference in the order given, not more -~0 94/14999 215 0 ~ ~ 5 PCTIUS93/12044 than 3.4, 2.0, 1.8, 1.3, or 1.0 g/L of NO3- ions.
It is to be understood that the specification of constituents in ionic form herein implies the presence of some counterions of opposite charge if needed to m~int~in chargeneutrality in the composition as a whole.
"Points" of free acid and total acid are defined for use herein as the number of millili~er.~ (hereinafter "ml") of 0.1 N NaOH solution required to titrate a 10 ml sample of the composition, to a phenolphth~l~.in end point (pH 9.0) for total acid and a bromthymol blue end point (pH 3.8) for free acid, except that if the composition has a pH greater than 3.8 initially, the points of free acid are defined as the negative of the number of ml of 0.1 N strong acid solution required to titrate a 10 ml sample of the composition to a pH of 3.8.
A process according to this invention comprises at a minimum a step of con-tacting a metal surface to be treated with a composition according to the invention for a sufficient time to form on the metal surface a detectable conversion coating. Con-ventional metal surface cl~ning and/or activation steps before contact between the metal to be treated and compositions according to the invention may be used if de-sired, and are generally preferred, as part of a process according to this invention. A
process according to the invention also may, and usually preferably does, include con-ventional steps subsequent to the contact between the metal surface to be treated and the compositiQnC according to the invention. These subsequent steps, e.g., may in-clude rinsing with water, any conventional reactive post treatments, e.g., with compo-sitions according to the te~hingc of U. S. Patent 4,963,596 or with chromate contain-ing solutions, and painting or otherwise protecting the surface with an outer coating of an organic based solid material.
Another embodiment of the invention is a concentrate composition, from which a working composition as deffned above can be prepared by dilution with water only, or by dilution with water and ~ tion of an unstable accelerator component such as nitrite ions.
Description of Preferred Embodiments of the Invention The phosphate ions required for the compositions according to this invention are preferably Po4-3 ions or other ions derivable from less complete ionization of ortho-WO 94/14999 215 0 5 ~ ~ PCT/US93112044 ~

phosphoric acid (H3PO4). Any free unionized phosphoric acid that may be present is considered part of the content of phosphate ions, to the extent of its stoichiometric cor-respondence to PO4~3 ions. Other free phosphoric acids such as metaphosphoric acid and condensed phosphoric acids such as pyrophosphoric acid and all anions derivable 6 from them may also be used to supply the necess~ry phosphate ions. Preferably the phosphate ions are derived from orthophosphoric acid and/or its neutral or acid salts of the metal cations also specified above as part of the compositions according to this invention.
The zinc cations required as part of the compositions are preferably derived from neutral or acid zinc salts of orthophosphoric acid, which may be formed in situ by dissolving zinc or zinc oxide or hydroxide in a solution containing the acid.The cupric cations required as part of the compositions according to this inven-tion may be derived from salts such as cupric sulfate and/or nitrate, or may be ob-tained by dissolving cupric oxide in part of the phosphoric acid used.
The accelerator component required in compositions according to the invention preferably incllldes at least one of the following: (i) from 0.01 to 0.2 g/l of nitrite ions, (ii) from 0.5 to 5 g/l of H2O2, (iii) from 0.05 to 2 g/l of m-nitroben7~.nP.sl11fonate ions, (iv) from 0.05 to 2 g/l of m-nitrobenzoate ions, (v) from 0.05 to 2 g/l of p-nitro-phenol, and (vi) from 0.1 to 10, more preferably from 0.5 to 6, or still more preferably from 0.5 to 2.0, g/L, measured as it stoichiometric equivalent as hydlo~ylamine, of a component capable of filrniching hydroxylamine in water solution. Most preferably, the accelerator is hydroxylamine sulfate (hereinafter often abbreviated "HAS") or a similar safe and readily available source of dissolved hydroxylamine. The secondmost preferable accelerator is nitrite ions.
The acidity of the compositions according to the invention is preferably derivedfrom phosphoric, sulfuric, and/or nitric acids.
Part or even all of the free fluori(le may be derived from complex fluoride ionssuch as fluoborate (BF4-2), fl~loh~fn~te (HflF6-2), fl~locilic~te (SiF6-2), fluotitanate (TiF6-2), fluozirconate (ZrF6-2), and mixtures thereof; more preferably, from fluoborate and fluo-silicate and mixtures thereof. However, simple fl~lori~les such as alkali metal fluorides are also entirely satisfactory sources of free fluoride.

~TVO 94/14999 215 0 5 4 ~ PCTlUS93/12044 -With increasing preference in the order given and with independent preference for each noted component, compositions according to the invention contain no more than 0.5, 0.2, 0.10, 0.07, 0.03, 0.01, 0.005, or 0.001 g/L of each of Ni~2, any cation with a valence of three or higher, chloride ions including complex chloride ions, and chlorate ions. Independently, if chloride ions are present in sufficient quantity to be readily determined analytically, it is preferred that the ratio of the concentration in glL
of complex fluoride ions to the concentration in g/L of chloride ions have a value of at least 8:1, or more preferably a value of at least 14:1.
In a process according to the invention, contact between the metal surface to be treated and a composition according to the invention may be accomplished by spraying, dipping, or any other convenient method or combination of methods. Thetemperature during contact between the metal treated and the composition according to the invention preferably is, with increasing preference in the order given, in the range from 21 to 85, 25 to 55, or 31 to 44, C. The total time of contact between the composition according to the invention and the metal surface to be conversion coated yreferably is, with increasing preference in the order given, in the range from 5 sec to 15 mimlt~s (hereinafter often abbreviated "min"), 15 seconds (hereinafter often abbreviated "sec") to 10 min, 30 sec to 5 min, or 90 to 120 sec. The add-on mass of the phosphate coating formed preferably is, with increasing preference in the order given, in the range from 1.1 to 5.4, 1.6 to 4.3, or 2.2 to 3.8, grams per square meter (hereinafter "g/m2) of surface treated. The weight percent of copper in the coat-ing formed preferably is, with increasing preference in the order given, from 0.50 to 10, 1.0 to 8.0, 2.0 to 6.0, 3.0 to 4.1.
Further appreciation of the present invention may be had from considering the following ex~mp]çs and comparative ex~mplçs which are intended to illustrate, but not limit, the invention.
Composition Examples and Comparison Examples Group I
These compositions, except for one comparison çx~mple, illustrate the use of HAS accelerator. Specific compositions are shown in Table 1 below. These composi-tions, except for comparison example 13 which was prepared from a commercially compounded concentrate, were prepared according to the following general procedure:

wo 94/14999 ~ Q ~ 4 5 PCT/US93/12044~

An amount of water equal to about three-quarters of the volume eventually desired for the composition was initially used, and an amount of zinc dihydrogen phosphate suffi-cient to provide the desired zinc ion concentration in the final desired volume was dis-solved in this water. An amount of 75 % aqueous solution of orthophosphoric acidthat was sufficient, together with the previously added zinc dihydrogen phosphate, to provide the desired final concentration of phosphate ions in the desired final volume was then added. Sufficient amounts of sodium fluoride to provide the desired fluoride ion content, of HAS to provide the desired hydroxylamine content and some sulfate, of cupric sulfate pentahydrate to provide the cupric ion and part of the sulfate ion con-tents, of m~n~nous nitrate to provide any desired m~ng~nese cation content, and of m~gnPcillm hydroxide or m~gnPsillm nitrate to provide any desired m~nesillm ion content were then added to the previously prepared solution in any order. Finally, the composition was adjusted with additions of sodium hydroxide solution and additional water as needed to produce the specified free acid and total acid concentrations.
Process Examples and Comparison Examples with Compositions of Group I
Test panels of cold rolled steel, galvanized steel, and/or conventional ~lllminllm alloys used in automobile and appliance m~nnf~ture were used and subjected to the following general sequence of process steps: (1) Conventional ~lk~line cleaner for 120 sec at 43 C, (2~ Water rinse at 38 C for 60 sec; (3) Conventional colloidal tit~ninm phosphate activator for 30 sec at 38 C; (4) Contact with one of Composi-tions 1 - 12 from Table 1 below for 120 sec at 35 C or at 43 C; (5) Cold water rinse at 20 - 25 C for 60 sec; (6) Post treatment for 30 sec with a conventional commer-cial post treatment composition cont~ining hexavalent and trivalent chromium; and (7) Rinse with deionized water for 30 sec at 20 - 25 C.

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Composition and Process Examples Group II
These compositions were prepared in the same general manner as for Group I, except that sodium nitrite instead of HAS was used as the accelerator and cupric ni-trate with an average of 2.5 molecules of water of hydration per cupric ion was used 5 as the copper source. Compositions are as follows:
Component ~/L of Component in:
Example 14 Example 15 Zn(NO3)2 4.74 3.6 75 % by weight aqueous H3PO4 12.4 20.4 ~o Cu(NO3)2 2% H2O 0.29 NaF , 1.1 1.5 NaNO2 0.12 0.11 Mn(NO3)2 2.3 Total Acid Points 17.0 18 Free Acid Points -0.3 0.4 Example 14 was used for spray phosphating at 33 C in a process sequence other-wise like those of Group I above. Example 14 was used for immersion phosphating at 57 C in a process sequence otherwise like those of Group I above.
20 Benefits of the Invention Not only were the cost reduction and pollution reduction objectives of the in-vention achieved, but also there were several unexpected and surprising benefits from the invention, at least in its most preferred embo~limentc Improved corrosion resist-ance, particularly to ~lk~lin~ corrosion; operation at a lower temperature than for con-25 ventional Zn-Ni-Mn phosphating compositions, with at least comp~r~ble and some-times better quality; better adhesion to paint applied over the conversion co~ting~c; and improved coatings on zinciferous surfaces such as galvanized steel.

Claims

1. An aqueous liquid composition consisting essentially of water and:
(A) from about 3 to about 50 g/L of dissolved phosphate ions;
(B) from about 0.2 to about 3 g/L of dissolved Zn+2 ions;
(C) from about 1 to about 200 mg/L of dissolved Cu+2 ions;
(D) an effective amount of a conventional accelerator exclusive of nitrate ions;(E) from about 5 to about 40 points of total acid; and (F) from about -1.0 to about +3.0 points of free acid; and, optionally, (G) up to about 2 g/L g/L in total of Mn+2 and Co+2 ions; and, optionally, (H) up to about 2 g/L of Mg+2 ions; and, optionally, (J) up to about 5.5 g/L of free fluoride as measured by a fluoride sensitive elec-trode; and, optionally, (K) not more than about 40 g/L of SO4-2 ions; and, optionally, (L) not more than about 4.5 g/L of NO3- ions; and, optionally, (M) not more than about 0.2 g/L of Ni+2 ions.

2. A composition according to claim 1, wherein:
(A) the amount of dissolved phosphate ions is from about 5 to about 20 g/L;
(B) the amount of dissolved Zn+2 ions is from about 0.45 to about 2.0 g/L;
(C) the amount of dissolved Cu+2 ions is from about 20 to about 100 mg/L;
(D) the accelerator includes at least one of (i) from about 0.01 to 0.2 g/l of nitrite ions, (ii) from about 0.5 to about 5 g/l of H2O2, (iii) from about 0.05 to about2 g/l of m-nitrobenzenesulfonate ions, (iv) from about 0.05 to about 2 g/l of m-nitrobenzoate ions, (v) from about 0.05 to about 2 g/l of p-nitrophenol, and (vi) from about 0.1 to about 10 g/L, measured as it stoichiometric equivalent as hydroxylamine, of a component capable of furnishing hydroxylamine in water solution;
(E) the "points" of total acid are from about 7 to about 25;
(F) the points of free acid are from about -0.5 to about +1.5;
(G) (i) the total concentration of Mn+2 and Co+2 ions is about 0.1 to about 0.8 g/L;
or (ii) the concentration of Mg+2 ions is from about 0.5 to about 1.0; or (iii) the concentrations of both the total of Mn+2 and Co+2 ions and of Mg+2 ions are within the ranges specified for the individual ions in parts (i) and (ii);
(J) the concentration of free fluoride as measured by a fluoride sensitive electrode is from about 1.0 to about 4.0 g/L;
(K) the concentration of SO4-2 ions is not more than about 11 g/L; and (L) the concentration of NO3- ions is not more than about 3.4 g/L.

3. A composition according to claim 2, wherein:
(B) the amount of dissolved Zn+2 ions is from about 0.57 to about 1.24 g/L;
(C) the amount of dissolved Cu+2 ions is from about 24 to about 74 mg/L;
(E) the "points" of total acid are from about 13 to about 24;
(F) the points of free acid are from about -0.5 to about +1.0; and (L) the concentration of NO3-ions is not more than about 2.0 g/L.

4. A composition according to claim 3, wherein:
(B) the amount of dissolved Zn+2 ions is from about 0.60 to about 0.95 g/L;
(D) the accelerator includes at least one of from about 0.01 to about 0.2 g/l ofnitrite ions and from about 0.5 to about 6 g/L, measured as it stoichiometric equivalent as hydroxylamine, of a component capable of furnishing hydroxylamine in water solution;
(E) the "points" of total acid are from about 16 to about 22;
(F) the points of free acid are from about 0.0 to about 0.8; and (L) the concentration of NO3- ions is not more than about 1.8 g/L.

5. A composition according to claim 3, wherein:
(B) the amount of dissolved Zn+2 ions is from about 0.60 to about 0.95 g/L;
(D) the accelerator includes at least one of from about 0.01 to about 0.2 g/l ofnitrite ions and from about 0.5 to about 6 g/L, measured as it stoichiometric equivalent as hydroxylamine, of a component capable of furnishing hydroxylamine in water solution;
(E) the "points" of total acid are from about 16 to about 22;
(F) the points of free acid are from about -0.5 to about 0.0; and (L) the concentration of NO3- ions is not more than about 1.8 g/L.

6. A composition according to claim 5, wherein:
(A) the amount of dissolved phosphate ions is from about 13 to about 18 g/L;
(B) the amount of dissolved Zn+2 ions is from about 0.71 to about 0.87 g/L;
(C) the amount of dissolved Cu+2 ions is from about 24 to about 60 mg/L;
(D) the accelerator includes at least one of from 0.01 to 0.2 g/l of nitrite ions and from about 0.5 to about 2 g/L, measured as it stoichiometric equivalent as hy-droxylamine, of HAS;
(E) the points of total acid are from about 18 to about 21;
(F) the points of free acid are from about -0.5 to about -0.2;
(G) (i) the concentration of the total of Mn+2 and Co+2 ions is from about 0.40 to about 0.65 g/L; or (ii) the concentration of Mg+2 ions is from about 0.70 to 0.80 g/L; or (iii) the concentration of both the total of Mn+2 and Co+2 ions andof Mg+2 ions are within the ranges already specified for the individual ions in items (G)(i) and (ii); and (L) the concentration of NO3- ions is not more than about 1.3 g/L.

7. A composition according to claim 4, wherein:
(A) the amount of dissolved phosphate ions is from about 13 to about 18 g/L;
(B) the amount of dissolved Zn+2 ions is from about 0.71 to about 0.87 g/L;
(C) the amount of dissolved Cu+2 ions is from about 24 to about 60 mg/L;
(D) the accelerator includes at least one of from 0.01 to 0.2 g/l of nitrite ions and from about 0.5 to about 2 g/L, measured as it stoichiometric equivalent as hy-droxylamine, of HAS;
(E) the points of total acid are from about 18 to about 21;
(F) the points of free acid are from about 0.35 to about 0.65;
(G) (i) the concentration of the total of Mn+2 and Co+2 ions is from about 0.40 to about 0.65 g/L; or (ii) the concentration of Mg+2 ions is from about 0.70 to 0.80 g/L; or (iii) the concentration of both the total of Mn+2 anc Co+2 ions andof Mg+2 ions are within the ranges already specified for the individual ions in items (G)(i) and (ii); and (L) the concentration of NO3- ions is not more than about 1.3 g/L.

8. A process for forming a phosphate coating on the surface of a metal substratethat does not include aluminum as part of its surface, wherein the surface of the sub-strate is contacted for a time within the range from about 90 to about 120 sec at a temperature within the range from about 40 to about 44 ° C with a composition ac-cording to claim 7, the add-on mass of the phosphate coating formed is in the range from about 2.2 to about 3.8 g/m2, and the weight percent of copper in the phosphate coating formed is within the range from about 3.0 to about 4.1.

9. A process for forming a phosphate coating on the surface of a metal substratethat includes aluminum as part of its surface, wherein the surface of the substrate is contacted for a time within the range from about 90 to about 120 sec at a temperature within the range from about 31 to about 44 ° C with a composition according to claim 6, the add-on mass of the phosphate coating formed is in the range from about 2.2 to about 3.8 g/m2, and the weight percent of copper in the phosphate coating formed is within the range from about 3.0 to about 4.1.

10. A process for forming a phosphate coating on the surface of a metal substrate that includes aluminum as part of its surface, wherein the surface of the substrate is contacted for a time within the range from about 30 sec to about 5 min at a tempera-ture within the range from about 25 to about 55 ° C with a composition according to claim 5, the add-on mass of the phosphate coating formed is in the range from about 1.6 to about 4.3 g/m2, and the weight percent of copper in the phosphate coatingformed is within the range from about 2.0 to about 6Ø

11. A process for forming a phosphate coating on the surface of a metal substrate that does not include aluminum as part of its surface, wherein the surface of the sub-strate is contacted for a time within the range from about 30 sec to about 5 min at a temperature within the range from about 40 to about 55 ° C with a composition ac-cording to claim 4, the add-on mass of the phosphate coating formed is in the range from about 1.6 to about 4.3 g/m2, and the weight percent of copper in the phosphate coating formed is within the range from about 2.0 to about 6Ø

12. A process for forming a phosphate coating on the surface of a metal substrate, wherein the surface of the substrate is contacted for a time within the range from about 15 sec to about 10 min at a temperature within the range from about 25 to about 55 ° C with a composition according to claim 3, the add-on mass of the phosphate coating formed is in the range from about 1.1 to about 5.4 g/m2, and the weight per-cent of copper in the phosphate coating formed is within the range from about 1.0 to about 8Ø

13. A process for forming a phosphate coating on the surface of a metal substrate, wherein the surface of the substrate is contacted for a time within the range from about 5 sec to about 15 min at a temperature within the range from about 21 to about 85 ° C with a composition according to claim 2, the add-on mass of the phosphate coating formed is in the range from about 1.1 to about 5.4 g/m2, and the weight per-cent of copper in the phosphate coating formed is within the range from about 0.50 to about 10Ø

14. A process for forming a phosphate coating on the surface of a metal substrate, wherein the surface of the substrate is contacted for a time within the range from about 5 sec to about 15 min at a temperature within the range from about 21 to about 85 ° C with a composition according to claim 1, the add-on mass of the phosphate coating formed is in the range from about 1.1 to about 5.4 g/m2, and the weight per-cent of copper in the phosphate coating formed is within the range from about 0.50 to about 10Ø

15. A process for forming a protective coating on the surface of a metal substrate, said process comprising steps of:
(1) cleaning the surface;
(2) contacting the cleaned surface with an activating composition containing colloidal titanium;
(3) forming a phosphate coating on the cleaned and activated surface by a process according to claim 14; and (4) applying an outer solid organic based coating over the phosphate coating formed in step (3).

16. A process for forming a protective coating on the surface of a metal substrate, said process comprising steps of:
(1) cleaning the surface;
(2) contacting the cleaned surface with an activating composition containing colloidal titanium;
(3) forming a phosphate coating on the cleaned and activated surface by a process according to claim 12; and (4) applying an outer solid organic based coating over the phosphate coating formed in step (3).

17. A process for forming a protective coating on the surface of a metal substrate that does not include aluminum as part of its surface, said process comprising steps of:
(1) cleaning the surface;
(2) contacting the cleaned surface with an activating composition containing colloidal titanium;
(3) forming a phosphate coating on the cleaned and activated surface by a process according to claim 11; and (4) applying an outer solid organic based coating over the phosphate coating formed in step (3).

18. A process for forming a protective coating on the surface of a metal substrate that includes aluminum as part of its surface, said process comprising steps of:(1) cleaning the surface;
(2) contacting the cleaned surface with an activating composition containing colloidal titanium;
(3) forming a phosphate coating on the cleaned and activated surface by a process according to claim 10; and (4) applying an outer solid organic based coating over the phosphate coating formed in step (3).

19. A process for forming a protective coating on the surface of a metal substrate that includes aluminum as part of its surface, said process comprising steps of:(1) cleaning the surface;
(2) contacting the cleaned surface with an activating composition containing colloidal titanium;
(3) forming a phosphate coating on the cleaned and activated surface by a process according to claim 9; and (4) applying an outer solid organic based coating over the phosphate coating formed in step (3).

20. A process for forming a protective coating on the surface of a metal substrate that does not include aluminum as part of its surface, said process comprising steps of:
(1) cleaning the surface;
(2) contacting the cleaned surface with an activating composition containing colloidal titanium;
(3) forming a phosphate coating on the cleaned and activated surface by a process according to claim 8; and (4) applying an outer solid organic based coating over the phosphate coating formed in step (3).