CCAΠ G CCMPGSΓΠCN AND METHOD FOR FORMING A SELF-HEALING CORROSION PREVENTATTVE

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BACKGROUND OF THE INVENTION ^"

(1) Field of the Invention :

The present invention pertains to coatings and metal surfac treatments preparatory to applying such coatings .

(2) Description of the Prior Art:

Many attempts have been made to improve the salt spra protection provided by protective coatings including among others improvements in compositions of coating materials and als pretreatments prior to coatings to modify the chemical surface fo better bond with the protective coating.

U. S. 2,528,535 to Merker teaches phosphating oil-in-wate systems for lubricating compositions, preferably with oxidatio inhibitors and mentions the possibility of adding and rust corrosio inhibitors, preferably less than 3% by weight.

U. S. 3 ,457, 173 to Pater lubricates metal surfaces by applyin siloxane-polyoxyalkylene block co-polymers .

Soviet Union Patent 0810782 teaches polymerized cotton seed oi apparently used as a lubricant.

U. S . Patent 4,440, 582 to Smith , et al. claims coatin compositions consisting essentially of phosphating oil , polysiloxan or alkylpolysiloxane and water and expresses a preference fo applying such coating compositions to metal parts which have bee phosphated .

None of the above references teach the surprising improvemen obtained by the present invention's use of sorbitan and preferabl also alkaline earth , e .g. barium, sulfonates .

It is particularly surprising that, in spite of the teaching of U.S . 4,440,582 that the compositions should consist essentially of (be restricted to) phosphating oils , silioxanes and water, the present invention involves the discovery that very substantial increases in performance can be obtained by adding one or more of the additional ingredients disclosed herein.

SUMMARY

(1) General Statement of the Invention:

The present invention, by using emulsions produced from oil-based concentrates comprising petroleum oils , siloxanes , and organic salts produced by reacting polyfunctional long chain organic compounds, e. g. polyamines or polyhydroxides or mixed polyamine/polyhydroxides with an organic acid provides when measured dramatically improved salt spray performance, particularly after car wash or contact with other detergent solutions . When applied over prepared ferrous metal surfaces, e. g. nitrided, chromated or phosphated ferrous metal work pieces , the compositions of the invention provide essentially self-healing polymer coatings , particularly suited for use in motor vehicles , military equipment, and all sorts of machinery. The invention is applicable to virtually any phosphated or nitrided work piece requiring substantial corrosion protection and can provide some . protection for even nonferrous workpieces.

(2) Utility of the Invention:

The invention is useful for protecting metals , particularly ferrous work pieces and especially those which have been previously phosphated or nitrided. While not wishing to be held to any theory of the invention, it appears that the nitriding or

phosphating increase the roughness of the metal surface , providing irregularities which more firmly grip and bond the coating layer to the metal work piece.

BRIEF DESCRIPTION OF THE DRAWING(S )

Figure 1 is a graph of salt-spray resistance (hours) for several inventive and conventional formulations .

Figure 2 is a schematic diagram of a manufacture according to the invention.

Figure 3 is a schematic diagram of a process of the present invention showing the phosphatizing followed by the dip coating into the emulsion compositions of the invention.

DESCRIPTION OF THE PREFERRED EMBODIMENT(S)

(1) Starting Materials:

A . Oil :

The oils useful in the present invention are petroleum-derived, with naphthenic oils being less preferred and paraffinic being more preferred. More preferable paraffinic oils include those having an SSU viscosity in the range of about 50 SSU to about 700, more preferably 100 to 400 and most preferably 250 to 370 seconds at 38°C (100°F) . Particularly preferred are oils having a viscosity index of above 90 , more preferably above 95.

The oil will preferably comprise from about 20 to 95 , more preferably 30 to 80 and most preferably 45 to 85 wt % of the total formulation of the invention concentrate .

B . Glycol Ether:

The invention comprises glycols , glycol ethers and derivatives thereof. Preferred are alkyl carbitols especially Butyl carbitol or most preferably, butyl cellosolve manufactured by Eastman Kodak, Rochester.

The glycols , etc . will preferably comprise from about 0.1 to 15 , more preferably 1 to 10 wt. % of the total formulation.

C. Emulsifying Agent:

The invention comprises emulsifying agents such as oxygenated hydrocarbons partially neutralized with alkaline earth metal (e. g. barium) then blended with alkali metal (e. g. sodium) sulfonates such as A OX575 available from ALOX Corp . of Niagara Falls or IDASOL D274 from Ideas , Inc. Woodale, IL, or similar products from N . L. Kimes , Inc. , Allison Park, PA.

The emulsifying agent will preferably comprise about 5 to 50, more preferably 8 to 35 , and most preferably 20 to 30 wt. % of the total formulation.

D . Siloxane:

Siloxanes useful in the present invention are substituted with one or more alkyl groups , each alkyl group comprising preferably 1 to stet, more preferably 1 to 6, and most preferably 1 to 5 carbon atoms .

These products are commercially available from Dow Chemical , Union Carbide, and other suppliers . These are produced from

silanes by condensation reactions to form a silica-oxygen-sil bound are as described in Dow brochure 22-240- A-78.

Preferred alkyl-substituted polysiloxanes are amino- unctio silicones, such as those described in U. S . patents 3 , 836 ,3 3 , 508,933, 3,890, 271 and 3 ,960 ,575.

The polysiloxanes will generally comprise from about 0.5 to wt. %, more preferably from 0.5 to 5 wt. % and most prefera from 1 to 4 wt. % of the concentrates of the present inventio

E. Water :

While the concentrate formations may contain 0.01 to 40 wt. or more of water (preferably demineralized) , 0.05 to 10 wt. % wa is preferred and 0.1 to 5 wt. % is most preferred. Emulsions generally contain about 50 to 95 wt. % water , or more , with 70 90% being more preferred.

F. Long Chain Organic Acid Salt ("Sorbitans") :

The polyoxyethylene derivative or fatty acid partial esters sorbitol anhydrides of the present invention are preferably sorbit derivatives and, without detracting from the generality, will be referred to throughout this application. Without being bound by a theory, it appears that these molecules, having a hydrophlic e which seeks water and a hydrophobic end which seeks oil , tend balance and couple the formulation into particularly sta emulsions . It is particularly surprising that, in addition, the sorbintan derivatives provide increased corrosion protecti performance.

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Preferred are the long chain polyfunctional organic compounds e .g. sorbitan monooleate , sorbitan trioleate, myristates with hydroxoy or amine polyfunctionality .

G. Organic Acid :

The organic acids which are a preferred but optional ingredient to the inventions of the present invention are preferably 12 to 54 carbon atoms , more preferably 14 to 20 and most preferably 18 (stearic) or isostearic and derivatives thereof .

Particularly preferred is isostearic acid which is liquid at room temperature. The organic acid may possibly somehow react with the amino functional polysiloxane ingredient of the compositions , but the function of the organic acid is not entirely clear. It is known that the addition of organic acid will, in most cases , substantially increase the stability of the concentrate and the performance of the resulting coatings .

From about 0.1 to 10, more preferably from about 0.5 to 5 and most preferably from about 1 to 4 wt. % of the total formulation will preferably be organic acid.

H. Metal Sulfonate:

A preferred feature of the present invention is the inclusion in the formulations of organic sulfonates . For best corrosion protection, it has been discovered that the preferred organic sulfonates are overbased (i.e. , made with an excess of calcium, barium or other metal carbonate) .

The preferred sulfonates are overbased with barium, calcium, potassium or sodium, and have sufficient equivalent weight to

provide extended rust protection against corrosive environments . The preferable equivalent weights of these sulfonates , which are derived from alkyl benzene, are as follows when overbased with the following metal sulfonates : sodium sulfonate or a equivalent weight preferably 370 to 750 , more preferably 400 to 650 and most preferably 450 to 600; barium sulfonate of a equivalent weight preferably 400 to 1400, more preferably 700 to 1300 , most preferably 800 to 1200 ; and calcium sulfonate of a equivalent weight preferably 370 to 850 , more preferably 400 to 800 , most preferably 500 to 750. A preferred commercial alkali metal sulfonate is Lubrizol 5530 manufactured by Lubrizol Corp . , Cleveland.

The organic sulfonates of the present invention will generally be employed in quantities of from about 1 to 60%, more preferably from about 5 to about 40% and most preferably from about 5 to about 30% based on the total weight of the formulation .

The preferred chain length is from about 10 to 30 , more preferably 12 to 24 and most preferably 16 to 20 carbon atoms . Molecular weights are preferably 10 to 50 , more preferably 15 to 40 and most preferably 20 to 30.

As mentioned above, the most preferred sorbitan derivative is sorbitan monooleate (molecular weight equals 465) , which is readily available under a number of brand names e. g. "Tweens" 20 through 85 , "Spans" 20 through 85 , "Sorbax" (by Chemax of Greenville , SC) , etc. from various suppliers , Atlas Chemical Division of ICI , Wilmington , DE , e .g. those described in McCutcheon "Emulsifiers and Detergents" , MC Pub . Co . , Glen Rock, NJ .

While the upper limits are primarily limited by economics , the sorbitan derivatives will generally be used in the formulations of

the invention at levels of about 0.1 to 20 wt. %, more preferably 0.5 to 15 and most preferably 1 to 10 weight percent.

I. A ine:

About 0.1 to 10 wt. % alkanol amine, preferably triethanol amine, may be added to provide additional wetability and stability where needed.

J. Miscellaneous Optional Additives:

Optional conventional ingredients might also be added, e . g. pigments , dyes , etc.

(2) Surface Treatment Processes :

Surface treatment processes can be conventional such as chromate, and particularly preferred nitriding or phosphating .

See generally Kirk and Othmer, "Encyclopedia of Chemical Technology, 2nd ed. , vol. 18 (1969) , pp 282-303 and the later editions .

Phosphating can be accomplished by the conventional techniques such as those set forth in "Practical Phosphate Coatings" , Mangill Company, and U. S . patents 3 ,967,948 , 2,465,247, 3,686,031 , 4,419, 199, 4,539,051 and 4,540,637 and references thereto. For automotive uses , preferred phosphating is to a thickness of at least 2000-3000 mg zinc phosphate/square foot of workpiece.

Nitriding can be either salt bath or fluidized bed nitriding , such as the commercial processes "Tuff Tride" , "Meionite" , "QPQ"

(Quench-Polish-Quench, in which salt bath nitriding is followed b quench in an oxidizing salt bath, followed by mechanical polishing and a second quench) , or fluidized bed nitriding as described i "Fluidized Bed Furnace Heat Treating Applications for the Dy Casting Industry" , JAPKA , May- June , 1983 , Dye Casting Engineer Miscellaneous surface treatment processes which may be employe with the invention include Procedyne's "Dyna-Case Surfac Hardening Treatment" , deep case carburization in a fluidize furnace by adding methanol which is vaporized and mixed wit nitrogen and a small amount of natural gas to form a syntheti endothermic atmosphere within the treating furnace at abou 899-1010°C (1650-1850°F) for 1-8 hours , carbonitriding at 815-871° (1500-1600°F) for 10 minutes-1 hour, followed by quenching nitriding by adding nitrogen from raw ammonia onto the surface o the material at 510-593 ^β C (950-1100 ^β F) to provide a case o 0.001-0.015 inches deep ; nitrαcarburizing providing a case o 0.0005-0.0020 inches deep by contacting mixtures of natural gas an raw ammonia in a fluid bed furnace at 566-621°C (1050-1150°F) fo 0.5-2 hours ; steam bluing in a fluid bed furnace at 343-538° (650-1000°F) for 20 minutes-1 hour to provide a blue or blac surface, or even combinations of these conventional surfac treatment processes .

(3) Concentrate Preparation :

Apparatus : The apparatus for the present invention will b that conventionally utilized in the preparation of coating compositions , e. g. kettles and mixing tanks having flow metering o measuring devices and agitation means , e. g. pumps mounted o side-arms connecting with the main vessel , internal stirrers , contra- rotating shearing devices and any of the other available devices which are well known to the art.

Temperature: The temperature during mixing may be different during different stages in the formulation. These temperatures are not narrowiy critical and will vary to provide faster mixing or better compatability of ingredients according to observation of those skilled in the art. For example, pressure vessels may be utilized for the purpose of lowering ingredient melting and boiling points , where useful, in order to provide better dispersion of difficult- to-mix ingredients .

Mixing Procedure: While the formulations of the present invention may be manufactured continuously if desired, batch techniques will be more usually employed. The sorbintan derivatives are then mixed in and the finished formulation is allowed to cook with, preferably, constant agitation, after which the formulation is drawn off into shipping containers , e.g. tank cars , tank trucks , drums or smaller cans.

Quality Control: The finished formulation , prior to packaging, will generally be checked for viscosity, freeze- thaw stability, corrosion-protection under accelerated conditions and other tests utilizing techniques well known to the coatings industry.

Application: The formulations of the present invention may be applied to substrates to be protected by conventional application techniques , such as spraying, brushing, dipping, flow-coating, dipspinning, "Filwhirl" , or airless spraying. Coating thickness can be varied by changing the formulation, the number of coats , or the amount applied per coat but in general will be in the range from about 2 to about 5 mils after drying.

(4) Emulsion Preparation:

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The concentrate (e . g . prepared according to Example 1 ) is diluted with 1 to 20 , or more preferably 2 to 15 , and most preferably 3 to 8 parts by weight of water to form the emulsion which is applied to the workpieces . Dilution is preferably about 38°C (100°F) , more preferably above 52°C • (125°F) , and most preferably at 52-71°C (125-160°F) .

(5) Batch or Continuous Basis :

While the examples describe the invention on a batch basis , it may come, of course, to be practiced on a continuous basis with continuous flows of starting materials into the mixing vessel and with continuous coating techniques e. g. roller coating continuous conveyor or even continuous work piece e . g . sheet steel moving continuously through a dip tank.

(8) Examples:

EXAMPLE I

(Formulation According to the Invention

Providing Excellent Salt Spray

Resistance and Shelf Life)

A conventional steam jacketed mixing kettle equipped with rotary stirrer are added 66 parts by weight of naphthanic oil having a viscosity of 100 SSU at 38°C (100°F) and purchased as McMillan and 100 VR which is heated to 54°C (130°F) . To the oil is added 20 parts by weight of emulsifying agent, ALOX 573 purchased from ALOX Corp . , Niagara Falls, 5 parts by weight in the form of butyl cellosolve from Eastman Kodak Company, Rochester, NY, 2 parts by weight sorbitan derivative as sorbitan monooleate purchased from Chemax Corp . of Greenville , SC , as sorbax SMO and 1 part by weight sodium sulfonate as an additional

emulsifier. Stirring continues during addition as a premixed composition purchased commercially, are added together 2.46 parts by weight polysiloxane as Dow 536, 2.46 parts by weight alkanolamide emulsifier as Witcamide 511 and 1.08 parts by weight of isostearic acid, although these could be added alternatively by reacting the isostearic acid with the polysiloxane . Heating is stopped but stirring is continued about 20 minutes to ensure a homogenious mixture. The contents of the mixing vessel are then sampled, quality control tests for viscosity , stability and appearance are run and the formulation is draw off into 55 gallon drums. (Water is not added separately because the individual ingredients contain about .5 parts by weight based on the weight of the total formulation of water. )

The resulting formulation is tested for corrosion protection by applying it to a ferrous work piece which has been previously phosphated by conventional techniques , by dipping the work piece into an emulsion formed by adding one part by volume of the above formulation with 4 parts by volume of demineralized water. After drying for 24 hours , the test work piece is subjected to a 5% neutral pH salt (NaCl) spray at a temperature of 35°C (95°F) according to ASTB-117. The test panel resists failure (corrosion) for 39 days (936 hours) .

A sample of the above formulation (undiluted) survives 5 successive freeze- fall cycles each comprising 16 hours at -18°C (0 ^β F) followed by 8 hours at 25°C (77°F) with no separation or other evident deleterious effects .

A sample of emulsion (diluted as specified above) shows no significant separation (i . e. , less than 2% "cream" ) upon standing at room temperature for 24 hours .

When a work piece as previously described is dipped into the above formulation (diluted) and allowed to dry at room temperature at approximately 50% relative humidity, the coating is cured and cured in 24 hours . But remains self-healing i. e . , scratch made with a scribe heals to protect the metal for about 24 hours .

(For comparison, a similar but unoiled phosphated workpiece fails in less than 48 hours and a similar but unoiled nitrided workpiece fails in less than 72 hours of salt spray . )

EXAMPLE II (Comparative According to U . S . 4 ,440,582)

When a formulation is prepared according to the techniques described in U. S . 4 ,440 ,582 by repeating the techniques of Example II below, but omitting the sorbitan monooleate (Chemax Sorbax SMO) and the emulsifying agent (ALOX 575) and retaining the oil , the amino functional silioxane (Dow 536) , the oil and the alkanolamide and issotearic acid and other ingredients in the parts by weight as specified in Table 1 , as tested similarly to the tests described in Example I , the work piece exposed to the same salt spray fails after 26 days (624 hours) , a reduction in salt spray failure time of about 33% as compared to the formulation of the present invention.

EXAMPLE III (Comparative- Without Silioxane)

When a formulation is prepared according to the techniques of Example I, but using as ingredients only oil, emulsifier (sodium sulfonate) , organic acid (oleic acid) , and triethanol amine , both an extra corrosion inhibitor (high molecular weight from Ideas , Inc . )

and a conventional defoamer from Diamond Shamrock, Morristown , NJ, the salt spray time failure is only 9 days (216 hours) .

EXAMPLE IV (According to the Invention but Omitting the Sorbitan Monooleate

Stabilizer)

When a formulation is prepared according to the techniques of Example 1 and using the same parts by weight except that the sorbitan monooleate stabilizer is omitted, the work piece treated with the diluted formulation in accordance with the techniques of Example 1 survives 38 days (816 hours) in the salt spray before failure, a substantial improvement over the comparative formulation of Example 2, but slightly less than the preferred formulation of Example 1. However, the formulation exhibits substantial separation during a 24 hour room temperature test on the undiluted concentrate.

EXAMPLE V (Invention, Substituting Paraffinic Oil)

When the techniques and tests of Example 1 are repeated but substituting a paraffinic oil for the naphthanic oil employed in Example 1, the resulting formulation survives 44 days (1056 hours) of salt spray test and the formulation is stable in both concentrated and emulsion form. This preferred formulation shows the superiority of the results obtained when paraffinic oil is substituted for naphthanic oil.

EXAMPLE VI

(Invention With Stabilizer,

Paraffinic Oil and Metal Sulfonate)

When a formulation is prepared according to the techniques of Example V, but additionally adding 10 parts by weight of a metai sulfonate as Lubrizol 5530, leaving further improved salt spray resistance of 54 days (1296 hours) to failure are observed . The formulation is stable in both the concentrated and emulsion forms . This Example illustrates the most preferred formulation of the invention with salt spray resistance of more than twice that of the prior art compared to the Example II .

EXAMPLES VII (Invention Used on Nitrided Workpiece)

When Example VI is repeated, substituting a nitrided workpiece for the phosphated workpiece, 42 days excellent protection is obtained, but the test is terminated before failure.

MODIFICATIONS

Specific compositions , methods , or embodiments discussed are intended to be only illustrative of the invention disclosed by this Specification. Variation on these compositions , methods , or embodiments are readily apparent to a person of skill in the art based upon the teachings of this specification and are therefore intended to be included as part of the inventions disclosed herein. For example, the formulation may contain biocides, antifoamers , dyes , pigments , etc.

Reference to patents made in the specification is intended to result in such patents being expressly incorporated herein by reference including any patents or other literature references cited within such patents .

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TABLE 1

EXAMPLE I II III IV V VI

Inv. Comp . Comp . fnv . Inv .

A. Oil

100 Pale 66 '6.1 83.5 330 Neutral 53.35 43 .35

B . Glycol

Butyl Cellosolve 5.0 1.0 5.0 4.8 4.8

C . Emulsifying Agent ALOX 575 20 28.5 27.4 1 . -±

D . Siloxane (aminofunctional silicone, Dow 536) 2.46 2.46 2.46 2.85 2.85

E . Water (demineralized)

F . "Sorbitan" Sorbitan monooleate 5.4 5.4

G. Organic Acid Oleic Acid 1.0 1.0 1.0 1.0

H. Metal Sulfonate Lubrizol 5530 10

I. Misc. Ingredients Sodium sulfonate 1 12 12 1.1 1.1 Witcomide 511 2.46 2.46 2.46 2.85 2.85 Isostearic Acid 1.08 1.08 1.08 1.25 1.25 Triethanolamine 1.5 1.0 High MW Sulfonate 2.0 2.0 Nopco NDW .5 .5

J. Tests

Salt Spray (days) 39 24 38 44 54

Stability (24 hrs) Concentrate pass pass pass fail pass pass Emulsion (20%) pass pass pass pass pass pass

Self Healing? yes yes no yes yes yes oily

* Nitrided workpiece; + = Test terminated before failure

TABLE 1 (con't)

EXAMPLE VII* Inv .

Oil

100 Pale

330 Neutral 53.35

B , Glycol

R . Cellosolve 4.8

Emulsifying Agent ALOX 575 27.4

D . Siloxane

(aminofunctional silicone , Dow 536) 2.85

E . Water (demineralized)

F . "Sorbitan" Sorbitan monooleate 5.4

Organic Acid Oleic Acid 1.0 H . Metal Sulfonate Lubrizol 5530

I . Misc . Ingredients Sodium sulfonate 1.1 Witcomide 511 2.85 Isosteric Acid 1.25 Triethanol Amine High MW Sulfonate Nopco NDW

Tests

Salt Spray (days) 42+

. Stability (24 hrs)

Concentrate pass

Emulsion (20%) pass

Self Healing? yes

* Nitrided workpiece ; + = Test terminated before failure