Cleaning and surface conditioning of formed metal surfaces

Abstract

A lubricant and surface conditioner for formed metal surfaces, particularly beverage containers, reduces the coefficient of static friction of said metal surfaces and enables drying said metal surfaces at a lower temperature. An aqueous composition for forming the conditioner by contact with metal surfaces includes a water-soluble organic material selected from a phosphate ester, alcohol, fatty acid including mono-, di-, tri-, and polyacids; fatty acid derivatives such as salts, hydroxy acids, amides, esters, ethers and derivatives thereof; and mixtures thereof and at least one of the elements selected from zirconium, titanium, cerium, aluminum, iron, tin, vanadium, tantalum, niobium, molybdenum, tungsten, and hafnium in metallic or ionic form. In order to avoid formation of sludge in the aqueous lubricant and surface conditioner forming composition, the composition should contain as little as possible of materials containing phenanthrene rings, such as conventional surfactants made by ethoxylating rosin. In order to assure the minimization of such surfactants in the aqueous lubricant and surface conditioner forming composition, surfactants containing phenanthrene rings should also be avoided or minimized in earlier cleaning stages.

Description

BACKGROUND OF THE INVENTION

1. Field of the Invention

This invention relates to a cleaner and surface conditioner for formed metal surfaces, and particularly, to such a lubricant and surface conditioner which improves the mobility of aluminum cans without adversely affecting the adhesion of paints or lacquers applied thereto, and also enables lowering the dryoff oven temperature required for drying said surfaces. Still more particularly, this invention relates to a combination of cleaning and such surface conditioning which minimizes the formation of sludge or other undesirable phase separation during the process of surface conditioning when the surface conditioner contains metallic elements as part of its chemical composition.

2. Discussion of Related Art

Aluminum cans are commonly used as containers for a wide variety of products. After their manufacture, the aluminum cans are typically washed with acidic cleaners to remove aluminum fines and other contaminants therefrom. Recently, environmental considerations and the possibility that residues remaining on the cans following acidic cleaning could influence the flavor of beverages packaged in the cans has led to an interest in alkaline cleaning to remove such fines and contaminants. However, the treatment of aluminum cans generally results in differential rates of metal surface etch on the outside versus on the inside of the cans. For example, optimum conditions required to attain an aluminum fines-free surface on the inside of the cans usually leads to can mobility problems on conveyors because of the increased roughness on the outside can surface.

These aluminum can mobility problems are particularly apparent when it is attempted to convey the cans through single filers and to printers. Thus, a need has arisen in the aluminum can manufacturing industry to modify the coefficient of static friction on the outside and inside surfaces of the cans to improve their mobility without adversely affecting the adhesion of paints or lacquers applied thereto. The reason for improving the mobility of aluminum cans is the general trend in this manufacturing industry to increase production without additional capital investments in building new plants. The increased production demand is requiring can manufacturers to increase their line and printer speeds to produce more cans per unit of time. For example, the maximum speed at which aluminum cans, in the absence of any treatment to reduce their coefficient of surface friction, may be passed through a printing station typically is on the average of about 1150 cans per minute, whereas it is desired that such rate be increased to about 1800 to 2000 cans per minute or even higher.

However, aluminum cans thoroughly cleaned by either acid or alkaline cleaners are, in general, characterized by high surface roughness and thus have a high coefficient of static friction. This property hinders the flow of cans through single filers and printers when attempting to increase their line speed. As a result, printer misfeeding problems, frequent jammings, down time, and loss of production occur in addition to high rates of can spoilage.

Another consideration in modifying the surface properties of aluminum cans is the concern that such modification may interfere with or adversely affect the ability of the can to be printed when passed to a printing or labeling station. For example, after cleaning the cans, labels may be printed on their outside surface, and lacquers may be sprayed on their inside surface. In such a case, the adhesion of the paints and lacquers is of major concern.

In addition, the current trend in the can manufacturing industry is directed toward using thinner gauges of aluminum metal stock. The down-gauging of aluminum can metal stock has caused a production problem in that, after washing, the cans require a lower drying oven temperature in order to pass the column strength pressure quality control test. However, lowering the drying oven temperature resulted in the cans not being dry enough when they reached the printing station, and caused label ink smears and a higher rate of can rejects.

Thus, it would be desirable to provide a means of improving the mobility of aluminum cans through single filers and printers to increase production, reduce line jammings, minimize down time, reduce can spoilage, improve ink laydown, and enable lowering the drying oven temperature of washed cans. Accordingly, it is an object of this invention to provide such means of improving the mobility of aluminum cans and to overcome the afore-noted problems.

In the most widely used current commercial practice, at least for large scale operations, aluminum cans are typically subjected to a succession of six cleaning and rinsing operations as described in Table A below. (Contact with ambient temperature tap water before any of the stages in Table A is sometimes used also; when used, this stage is often called a "vestibule" to the numbered stages.)

TABLE A______________________________________STAGENUMBER ACTION ON SURFACE DURING STAGE______________________________________1 Aqueous Acid Precleaning2 Aqueous Acid and Surfactant Cleaning3 Tap Water Rinse4 Mild Acid Postcleaning, Conversion Coating, or Tap Water Rinse5 Tap Water Rinse6 Deionized ("DI") Water Rinse______________________________________

It is currently possible to produce a can which is satisfactorily mobile and to which subsequently applied inks and/or lacquers have adequate adhesion by using suitable surfactants either in Stage 4 or Stage 6 as noted above. Preferred treatments for use in Stage 4 as described above have been developed and are described in U.S. Pat. Nos. 5,030,323 and 5,064,500. With these treatments, a metallic element (not necessarily or even usually in elemental form) is incorporated into the lubricant and surface conditioning layer formed.

Experience with prolonged practical use of lubricant and surface conditioner forming treatments that incorporate metal into the surface conditioner layer formed has revealed that they are susceptible to the development of at least one separate impurity phase, commonly called "sludge" or some similar term. The sludge is usually sticky, so that small particles of it easily adhere to the containers being treated, and if they do so can cause an undesirable phenomenon called "metal exposure", a failure of the subsequently applied interior sanitary lacquer to completely isolate the beverage product contained in the aluminum can from contact with the metal can body. Therefore, if a sufficient amount of sludge forms, it must be removed before continuing with can conditioning. Because of the tackiness of the sludge, it is difficult to remove satisfactorily, so that minimizing and, if possible, preventing formation of the sludge is one of the objects of this invention.

DESCRIPTION OF THE INVENTION

Other than in the claims and the operating examples, or where otherwise expressly indicated, all numbers expressing quantities of ingredients or reaction conditions used herein are to be understood as modified in all instances by the term "about" in describing the broadest scope of the invention. Practice within the numerical limits given, however, is generally preferred. Also, unless otherwise specified, all descriptions of components of compositions by percentages, "parts", or the like refer to weight or mass of the component compared with the total.

In accordance with this invention, it has been found that a lubricant and surface conditioner applied to aluminum cans after washing enhances their mobility and, in a preferred embodiment, improves their water film drainage and evaporation characteristics as to enable lowering the temperature of a drying oven by from about 25.degree. to about 100.degree. F. without having any adverse effect on the label printing process. The lubricant and surface conditioner reduces the coefficient of static friction on the outside surface of the cans, enabling a substantial increase in production line speeds, and in addition, provides a noticeable improvement in the rate of water film drainage and evaporation resulting in savings due to lower energy demands while meeting quality control requirements.

More particularly, in accordance with one preferred embodiment of this invention, it has been found that application of a thin organic film to the outside surface of aluminum cans serves as a lubricant inducing thereto a lower coefficient of static friction, which consequently provides an improved mobility to the cans, and also increases the rate at which the cans may be dried and still pass the quality control column strength pressure test. It has also been found that the degree of improved mobility and drying rate of the cans depends on the thickness or amount of the organic film, and on the chemical nature of the material applied to the cans.

The lubricant and surface conditioner for aluminum cans in accordance with this invention may, for example, be selected from water-soluble alkoxylated surfactants such as organic phosphate esters; alcohols; fatty acids including mono-, di-, tri-, and poly-acids; fatty acid derivatives such as salts, hydroxy acids, amides, esters, ethers and derivatives thereof; and mixtures thereof.

The lubricant and surface conditioner for aluminum cans in accordance with this invention in one embodiment preferably comprises a water-soluble derivative of a saturated fatty acid such as an ethoxylated stearic acid or an ethoxylated isostearic acid, or alkali metal salts thereof such as polyoxyethylated stearate and polyoxyethylated isostearate. Alternatively, the lubricant and surface conditioner for aluminum cans may comprise a water-soluble alcohol having at least about 4 carbon atoms and may contain up to about 50 moles of ethylene oxide. Excellent results have been obtained when the alcohol comprises polyoxyethylated oleyl alcohol containing an average of about 20 moles of ethylene oxide per mole of alcohol.

In another preferred aspect of this invention, the organic material employed to form a film on an aluminum can following alkaline or acid cleaning and prior to the last drying of the exterior surface prior to conveying comprises a water-soluble organic material selected from a phosphate ester, an alcohol, fatty acids including mono-, di-, tri-, and poly-acids fatty acid derivates including salts, hydroxy acids, amides, alcohols, esters, ethers and derivatives thereof and mixtures thereof. Such organic material is preferably part of an aqueous solution comprising water-soluble organic material suitable for forming a film on the cleaned aluminum can to provide the surface after drying with a coefficient of static friction not more than 1.5 and that is less than would be obtained on a can surface of the same type without such film coating.

In one embodiment of the invention, water solubility can be imparted to organic materials by alkoxylation, preferably ethoxylation, propoxylation or mixture thereof. However, non-alkoxylated phosphate esters are also useful in the present invention, especially free acid containing or neutralized mono-and diesters of phosphoric acid with various alcohols. Specific examples include Tryfac.RTM. 5573 Phosphate Ester, a free acid containing ester available from Henkel Corp.; and Triton.RTM. H-55, Triton.RTM. H-66, and Triton.RTM. QS-44, all available from Union Carbide Corporation.

Preferred non-ethoxylated alcohols include the following classes of alcohols:

Suitable monohydric alcohols and their esters with inorganic acids include water soluble compounds containing from 3 to about 20 carbons per molecule. Specific examples include sodium lauryl sulfates such as Duponol.RTM. WAQ and Duponol.RTM. QC and Duponol.RTM. WA and Duponol.RTM. C available from Witco Corp. and proprietary sodium alkyl sulfonates such as Alkanol.RTM.189-S available from E. I. du Pont de Nemours & Co.

Suitable polyhydric alcohols include aliphatic or arylalkyl polyhydric alcohols containing two or more hydroxyl groups. Specific examples include glycerine, sorbitol, mannitol, xanthan gum, hexylene glycol, gluconic acid, gluconate salts, glucoheptonate salts, pentaerythritol and derivatives thereof, sugars, and alkylpolyglycosides such as APG.RTM.300 and APG.RTM.325, available from Henkel Corp. Especially preferred polyhydric alcohols include triglycerols, especially glycerine or fatty acid esters thereof such as castor oil triglycerides.

In accordance with the present invention, we have discovered that employing alkoxylated, especially ethoxylated, castor oil triglycerides as lubricants and surface conditioners results in further improvements in can mobility especially where operation of the can line is interrupted causing the cans to be exposed to elevated temperatures for extended periods. Accordingly, especially preferred materials include Trylox.RTM. 5900, Trylox.RTM. 5902, Trylox.RTM. 5904, Trylox.RTM. 5906, Trylox.RTM. 5907, Trylox.RTM. 5909, Trylox.RTM. 5918, and hydrogenated castor oil derivatives such as Trylox.RTM. 5921 and Trylox.RTM. 5922, all available from Henkel Corp.

Preferred fatty acids include butyric, valeric, caproic, caprylic, capric, pelargonic, lauric, myristic, palmitic, oleic, stearic, linoleic, and ricinoleic acids; malonic, succinic, glutaric, adipic, maleic, tartaric, gluconic, and dimer acids; and salts of any of these; iminodipropionate salts such as Amphoteric N and Amphoteric 400 available from Exxon Chemical Co.; sulfosuccinate derivatives such as Texapor.RTM.SH-135 Special and Texapon.RTM.SB-3, available from Henkel Corp.; citric, nitrilotriacetic, and trimellitic acids; Cheelox.RTM. HEEDTA, N-(hydroxyethyl)ethylenediaminetriacetate, available from GAF Chemicals Corp.

Preferred amides generally include amides or substituted amides of carboxylic acids having from four to twenty carbons. Specific examples are Alkamide.RTM. L203 lauric monoethanolamide, Alkamide.RTM. L7DE lauric/myristic alkanolamide, Alkamide.RTM. DS 280/s stearic diethanolamide, Alkamide.RTM. CD coconut diethanolamide, Alkamide.RTM. DIN 100 lauric/linoleic diethanolamide, Alkamide.RTM. DIN 295/s linoleic diethanolamide, Alkamide.RTM. DL 203 lauric diethanolamide, all available from Rhone-Poulenc; Monamid.RTM. 150-MW myristic ethanolamide, Monamid.RTM. 150-CW capric ethanolamide, Monamid.RTM. 150-1S isostearic ethanolamide, all available from Mona Industries Inc.; and Ethomid.RTM. HT/23 and Ethomid.RTM. HT60 polyoxyethylated hydrogenated tallow amines, available from Akzo Chemicals Inc.

Preferred anionic organic derivatives generally include sulfate and sulfonate derivates of fatty acids including sulfate and sulfonate derivatives of natural and synthetically derived alcohols, acids and natural products. Specific examples include: dodecyl benzene sulfonates such as Dowfax.RTM. 2A1, Dowfax.RTM. 2AO, Dowfax.RTM. 3BO, and Dowfax.RTM. 3B2, all available from Dow Chemical Co.; Lomar.RTM. LS condensed naphthalene sulfonic acid, potassium salt available from Henkel Corp.; sulfosuccinate derivatives such as Monamate.RTM. CPA sodium sulfosuccinate of a modified alkanolamide, Monamate.RTM. LA-100 disodium lauryl sulfosuccinate, all available from Mona Industries; Triton.RTM. GR-5M sodium dioctylsulfosuccinate, available from Union Carbide Chemical and Plastics Co.; Varsulf.RTM. SBFA 30, fatty alcohol ether sulfosuccinate, Varsulf.RTM. SBL 203, fatty acid alkanolamide sulfosuccinate, Varsulf.RTM. S1333, ricinoleic monoethanolamide sulfosuccinate, all available from Sherex Chemical Co., Inc.

Another preferred group of organic materials comprise water-soluble alkoxylated, preferably ethoxylated, propoxylated, or mixed ethoxylated and propoxylated materials, most preferably ethoxylated, and non-ethoxylated organic materials selected from amine salts of fatty acids including mono-, di-, tri-, and poly-acids, amino fatty acids, fatty amine N-oxides, and quaternary salts, and water soluble polymers.

Preferred amine salts of fatty acids include ammonium, quaternary ammonium, phosphonium, and alkali metal salts of fatty acids and derivatives thereof containing up to 50 moles of alkylene oxide in either or both the cationic or anionic species. Specific examples include Amphoteric N and Amphoteric 400 iminodipropionate sodium salts, available from Exxon Chemical Co.; Deriphat.RTM. 154 disodium N-tallow-beta iminodipropionate and Deriphat.RTM. 160, disodium N-laurylbeta iminodipropionate, available from Henkel Corp.

Preferred amino acids include alpha and beta amino acids and diacids and salts thereof, including alkyl and alkoxyiminodipropionic acids and their salts and sarcosine derivatives and their salts. Specific examples include Armeen.RTM. Z, N-coco-betaoaminobutyric acid, available from Akzo Chemicals Inc.; Amphoteric N, Amphoteric 400, Exxon Chemical Co.; sarcosine (N-methyl glycine); hydroxyethyl glycine; Hamposyl.RTM. TL-40 triethanolamine lauroyl sarcosinate, Hamposyl.RTM. O oleyl sarcosinate, Hamposyl.RTM. AL-30 ammoniumlauroyl sarcosinate, Hamposyl.RTM. L lauroyl sarcosinate, and Hamposyl.RTM. C cocoyl sarcosinate, all available from W. R. Grace & Co.

Preferred amine N-oxides include amine oxides where at least one alkyl substituent contains at least three carbons and up to 20 carbons. Specific examples include Aromox.RTM. C/12 bis-(2-hydroxyethyl)cocoalkylamine oxide, Aromox.RTM. T/12 bis-(2-hydroxyethyl)tallowalkylamine oxide, Aromox.RTM. DMC dimethylcocoalkylamine oxide, Aromox.RTM. DMHT hydrogenated dimethyltallowalkylamine oxide, Aromox.RTM.DM-16 dimethylheaxdecylalkylamine oxide, all available from Akzo Chemicals Inc.; and Tomah.RTM. AO-14-2 and Tomah.RTM. AO-728 available from Exxon Chemical Co.

Preferred quaternary salts include quaternary ammonium derivatives of fatty amines containing at least one substituent containing from 12 to 20 carbon atoms and zero to 50 moles of ethylene oxide and/or zero to 15 moles of propylene oxide where the counter ion consists of halide, sulfate, nitrate, carboxylate, alkyl or aryl sulfate, alkyl or aryl sulfonate or derivatives thereof. Specific examples include Arquad.RTM. 12-37W dodecyltrimethylammonium chloride, Arquad.RTM. 18-50 octadecyltrimethylammonium chloride, Arquad.RTM. 210-50 didecyldimethylammonium chloride, Arquad.RTM. 218-100 dioctadecyldimethylammonium chloride, Arquad.RTM. 316(W) trihexadecylmethylammonium chloride, Arquad.RTM. B-100 benzyldimethyl( C.sub.12-18)alkylammonium chloride, Ethoquad.RTM. C/12 cocomethyl[POE (2)]ammonium chloride, Ethoquad.RTM. C/25 cocomethyl[POE(15)]ammonium chloride, Ethoquad.RTM. C/12 nitrate salt, Ethoquad.RTM. T/13 Acetate tris(2-hydroxyethyl)tallowalkyl ammonium acetate, Duoqaude T-50 N,N,N',N',N'-pentamethyl-N-tallow-1,3-diammonium dichloride, Propoquad.RTM. 2HT/11 di(hydrogenated tallowalkyl)(2-hydroxy-2-methylethyl)methylammonium chloride, Propoquad.RTM.T/12 tallowalkylmethyl-bis-(2-hydroxy-2-methylethyl)ammonium methyl sulfate, all available from Akzo Chemicals Inc.; Monaquate P-TS stearamidopropyl PG-dimonium chloride phosphate, available from Mona Industries Inc.; Chemquate 12-33 lauryltrimethylammonium chloride, Chemquate 16-50 Cetyltrimethylammonium chloride available from Chemax Inc.; and tetraethylammonium pelargonate, laurate, myristate, oleate, stearate or isostearate.

Preferred water-soluble polymers include homopolymers and heteropolymers of ethylene oxide, propylene oxide, butylene oxide, acrylic acid and its derivatives, maleic acid and its derivatives, vinyl phenol and its derivatives, and vinyl alcohol. Specific examples include Carbowax.RTM. 200, Carbowax.RTM. 600, Carbowax.RTM. 900, Carbowax.RTM. 1450, Carbowax.RTM. 3350, Carbowax.RTM. 8000, and Compound 20M, all available from Union Carbide Corp.; Pluronic.RTM. L61, Plutonic.RTM. L81, Pluronic.RTM. 31R1, Pluronic.RTM. 25R2, Tetronic.RTM. 304, Tetronic.RTM. 701, Tetronic.RTM. 908, Tetronic.RTM. 90R4, and Tetronic.RTM. 150R1, all available from BASF Wyandotte Corp.; Acusol.RTM. 410N sodium salt of polyacrylic acid, Acusol.RTM. 445 polyacrylic acid, Acusol.RTM. 460ND sodium salt of maleic acid/olefin copolymer, and Acusol.RTM. 479N sodium salt of acrylic acid/maleic acid copolymer, all available from Rohm & Haas Company; and N-methylglucamine adducts of polyvinylphenol and N-methylethanolamine adducts of polyvinylphenol.

Additional improvements are achieved by combining with the organic material(s) noted above an inorganic material selected from metallic or ionic zirconium, titanium, cerium, aluminum, iron, vanadium, tantalum, niobium, molybdenum, tungsten, hafnium or tin to produce a film combining one or more of these metals with one or more of the above-described organic materials. A thin film is produced having a coefficient of static friction that is not more than 1.5 and is less than the coefficient without such film, thereby improving can mobility in high speed conveying without interfering with subsequent lacquering, other painting, printing, or other similar decorating of the containers. This type of lubricant and surface conditioner is especially preferred when used in Stage 4 as defined above.

The technique of incorporating such inorganic materials is described, in particular detail with reference to zirconium containing materials, in U.S. Pat. Nos. 5,030,323 of Jul. 9, 1991 and 5,064,500 of Nov. 12, 1991, the entire disclosures of which, to the extent not inconsistent with any explicit statement herein, are hereby incorporated herein by reference. The substitution of other metallic materials for those taught explicitly in one of these patents is within the scope of those skilled in the art.

In a further preferred embodiment of the process of the present invention, in order to provide improved water solubility, especially for the non-ethoxylated organic materials described herein, and to produce a suitable film on the can surface having a coefficient of static friction not more than 1.5 after drying, one employs a lubricant and surface conditioner forming composition that includes one or more surfactants, preferably alkoxylated and most preferably ethoxylated, along with such non-ethoxylated organic material to contact the cleaned can surface prior to final drying and conveying. Preferred surfactants include ethoxylated and non-ethoxylated sulfated or sulfonated fatty alcohols, such as lauryl and coco alcohols. Suitable are a wide class of anionic, non-ionic, cationic, or amphoteric surfactants. Alkyl polyglycosides such as C.sub.8 -C.sub.48 alkyl polyglycosides having average degrees of polymerization between 1.2 and 2.0 are also suitable. Other classes of surfactants suitable in combination are ethoxylated nonyl and octyl phenols containing from 1.5 to 100 moles of ethylene oxide, preferably a nonylphenol condensed with from 6 to 50 moles of ethylene oxide such as Igepale) CO-887 available from Rhone-Poulenc; alkyl/aryl polyethers, for example, Triton.RTM. DF-16; and phosphate esters of which Tritone) H-66 and Triton.RTM. QS-44 are examples, all of the Triton.RTM. products being available from Union Carbide Co., and Ethox.RTM. 2684 and Ethfac.RTM. 136, both available from Ethox Chemicals Inc., are representative examples; polyethoxylated and/or polypropoxylated derivatives of linear and branched alcohols and derivatives thereof, as for example Trycol.RTM. 6720 (Henkel Corp.), Surfonic.RTM. LF-17 (Huntsman Chemical Co.) and Antarox.RTM. LF-330 (Rhone-Poulenc); sulfonated derivatives of linear or branched aliphatic alcohols, for example, Neodol.RTM. 25-3S (Shell Chemical Co.); sulfonated aryl derivatives, for example, Dyasulf.RTM. 9268-A, Dyasulf.RTM. C-70, Lomar.RTM. D (Henkel Corp.) and Dowfax.RTM. 2A1 (Dow Chemical Co.); and ethylene oxide and propylene oxide copolymers, for example, Pluronic.RTM. L-61, Pluronic.RTM. 81, Pluronic.RTM. 31R1, Tetronic.RTM. 701, Tetronic.RTM. 90R4 and Tetronic.RTM. 150R1, all available from BASF Corp.

Surprisingly, it has been found that surfactants containing a phenanthrene ring structure, which is to be understood herein as contained not only in phenanthrene itself but in molecules made by hydrogenating phenanthrene to any degree not sufficient to break any of the three rings present in phenanthrene, are disadvantageous constituents of the lubricant and surface conditioner forming composition, at least if this composition also contains any inorganic material selected from metallic or ionic zirconium, titanium, cerium, aluminum, iron, vanadium, tantalum, niobium, molybdenum, tungsten, hafnium or tin as described above. The formation of sludge is notably increased when such surfactants are present together with any of these inorganic materials. It has also been found that the tendency to sludge formation can usefully be tested in a laboratory, without the need for actual can processing, by deliberately adding such soils as aluminum fines, soluble aluminum-containing species, drawing oils, and cleaner surfactants to the lubricant and surface conditioner forming composition to be tested for resistance to sludging, then passing the deliberately soiled composition through a spraying stage repeatedly and observing whether any dry floc is visible on the head of foam that forms in the container into which the spray drains. The presence or absence of dry FDIC in this test indicates, with at least rough quantitative correlation, whether or not sludge will likely become a problem in operating the lubricant and surface conditioner forming composition thus tested, and if so, the extent of the sludge formation likely to be observed in practical use.

Surfactants with a phenanthrene ring structure, especially abietate, hydrogenated abietate, and alkoxylated abietate surfactants derived from natural rosin, are very commonly used now in the cleaning stage of container processing, before contact with any lubricant and surface conditioner forming composition, for example in Stage 2 as shown in Table A. Inasmuch as carry-over of some of the cleaner surfactants into the compositions used for later stages of treatment can not be entirely avoided in practical high speed and high volume can processing, such cleaner surfactants should be used only with care and in limited amounts if at all in any processing stage prior to a lubricant and surface conditioner forming composition that includes inorganic material selected from metallic or ionic zirconium, titanium, cerium, aluminum, iron, vanadium, tantalum, niobium, molybdenum, tungsten, hafnium or tin as described above.

More specifically, it is preferred, with increasing preference in the order given and independently for each composition concerned, that (i) any lubricant and surface conditioner forming composition that contains inorganic material selected from metallic or ionic zirconium, titanium, cerium, aluminum, iron, vanadium, tantalum, niobium, molybdenum, tungsten, hafnium or tin as described above and (11) any cleaner or rinse composition that is contacted with the containers to be provided with a lubricant and surface conditioner layer before the containers are brought into contact with the lubricant and surface conditioner forming composition, should contain not more than 5, 4, 3, 2, 1, 0.5, 0.4, 0.3, 0.2, 0.1, 0.05, 0.04, 0.03, 0.02, 0.01, 0.005, 0.004, 0.003, 0.002, 0.001, 0.0005, 0.0004, 0.0003, 0.0002, 0.0001, 0.00005, 0.00004, 0.00003, 0.00002, or 0.00001% in total of carbon atoms that are part of a phenanthrene ring structure as defined above. The minimization of concentration of phenanthrene ring containing compounds is particularly advantageous in connection with the use of lubricant and surface conditioner forming compositions as taught in U.S. Pat. Nos. 5,030,323 and 5,064,500

Phenanthrene ring containing nonionic surfactants have been extensively used for at least the last several years for cleaning aluminum containers, because they are highly effective in removing some of the kinds of organic soils often found on such containers. However, it has now been found that alkyl phenol based nonionic surfactants can satisfactorily replace phenanthrene ring containing surfactants for this purpose, and the alkyl phenol based surfactants do not promote sludge formation in metal containing lubricant and surface conditioner forming compositions as do phenanthrene ring containing surfactants. A particularly preferred combination of surfactants for a cleaner stage preceding a metal containing lubricant and surface conditioner forming compositions comprises, more preferably consists essentially of, or still more preferably consists of:

(A) a component of nonionic surfactants selected from the group consisting of surfactants corresponding to the chemical formula: ##STR1## where a is 0 or 1; R represents an alkyl moiety that may be branched or unbranched and saturated or unsaturated but does not include any aryl group and the sum of a plus the number of carbon atoms in R is from 10-22, more preferably from 12-20, or still more preferably from 14-18; n is an integer that is at least 2 and is not greater than 4, more preferably not greater than 3, most preferably 2 and may be different from one C.sub.n H.sub.2n O group to another in the same molecule; and b is an integer, the value or values of b being selected such that the hydrophile-lipophile balance ("HLB") of the total component is, with increasing preference in the order given, not less than 8, 10, 10.5, 11.0, 11.3, 11.5, 11.7, 11.8, 11.9, 12.0, or 12.1 and independently is, with increasing preference in the order given, not more than 20, 18, 16, 15, 14, 13.7, 13.5, 13.3, 13.1, 12.9, 12.8, 12.7, 12.6, 12.5, 12.4, or 12.3; and (B) a component of nonionic surfactants selected from the group consisting of surfactants corresponding to the chemical formula R'-.phi.-(C.sub.n H.sub.2n O).sub.c H, where R' represents an alkyl moiety that may be branched or unbranched and saturated or unsaturated but does not include any aryl group and that has from 4-16, more preferably from 6-14, still more preferably from 8-10, most preferably 9, carbon atoms; .phi. represents a phenylene group; n is an integer that is at least 2 and is not greater than 4, more preferably not greater than 3, most preferably 2; and c is an integer, the value or values of c being selected such that the HLB of the total component is, with increasing preference in the order given, not less than 9, 10.0, 10.6 11.2, 11.7, 12.2, 12.5, 12.7, 12.9, 13.0, 13.1, 13.2, or 13.3 and independently is, with increasing preference in the order given, not more than 21, 19, 17, 16, 15, 14.7, 14.5, 14.3, 14.1, 13.9, 13.8, 13.7, 13.6, or 13.5. Independently, the ratio of component (A) to component (B) in the mixture preferably is, with increasing preference in the order given, not less than 0.1, 0.2, 0.3, 0.4, 0.5, 0.55, 0.59, 0.63, 0.60, 0.62, 0.64, 0.66, 0.67, 0.68, 0.69, 0.70, or 0.71 and independently preferably is, with increasing preference in the order given, not greater than 10, 5, 4, 3, 2, 1.5, 1.2, 1.1, 1.0, 0.9, 0.85, 0.83, 0.81, 0.80, 0.79, 0.78, 0.77, 0.76, 0.75, 0.74, 0.73, or 0.72.

The lubricant and surface conditioner for aluminum cans in accordance with this invention may comprise a phosphate acid ester or preferably an ethoxylated alkyl alcohol phosphate ester. Such phosphate esters are commercially available as Gafac.RTM. PE 510 from GAF Corporation, Wayne, N.J., and as Ethfac.RTM. 136 and 161 and Ethox.RTM. 2684 from Ethox Chemicals, Inc., Greeneville, S.C. In general, the organic phosphate esters may comprise alkyl and aryl phosphate esters with and without ethoxylation.

The lubricant and surface conditioner forming composition for aluminum cans may be applied to the cans during their wash cycle, during one of their treatment cycles such as cleaning or conversion coating, during one of their water rinse cycles, or during their final water rinse cycle. In addition, the lubricant and surface conditioner may be applied to the cans after their final water rinse cycle, i.e., prior to oven drying, or after oven drying, by fine mist application from water or another volatile non-inflammable solvent solution. It has been found that the lubricant and surface conditioner is capable of depositing on the aluminum surface of the cans to provide them with the desired characteristics. The lubricant and surface conditioner may be applied by spraying and reacts with the aluminum surface through chemisorption or physiosorption to provide it with the desired film.

Generally, in the cleaning process of the cans, after the cans have been washed, they are typically exposed to an acidic water rinse. In accordance with this invention, the cans may thereafter be treated with a lubricant and surface conditioner comprising an anionic surfactant such as a phosphate acid ester. In such case, the pH of the treatment system is important and generally should be acidic, that is between about 1 and about 6.5, preferably between about 2.5 and about 5. If the cans are not treated with the lubricant and surface conditioner of this invention next after the acidic water rinse, the cans are often exposed to a tap water rinse and then to a deionized water rinse. In such event, the deionized water rinse solution is prepared to contain the lubricant and surface conditioner forming composition of this invention, which may comprise a nonionic surfactant selected from the aforementioned polyoxyethylated alcohols or polyoxyethylated fatty acids, or any of the other suitable materials as described above. After such treatment, the cans may be passed to an oven for drying prior to further processing.

The amount of lubricant and surface conditioner to be applied to the cans should be sufficient to reduce the coefficient of static friction on the outside surface of the cans to a value of about 1.5 or lower, and preferably to a value of about 1 or lower. Generally speaking, such amount should be on the order of from about 3 mg/m.sup.2 to about 60 mg/m.sup.2 of lubricant and surface conditioner on the outside surface of the cans.

Another embodiment of the present invention comprises the application of the technology described herein to providing lubricants and surface conditioners for tin-cans especially to aid in dewatering and drying of such cans. The compositions and methods described herein are suitable for that purpose.

For a fuller appreciation of the invention, reference may be made to the following examples, which are intended to be merely descriptive, illustrative, and not limiting as to the scope of the invention.

EXAMPLE 1

This example illustrates the amount of aluminum can lubricant and surface conditioner necessary to improve the mobility of the cans through the tracks and printing stations of an industrial can manufacturing facility, and also shows that the lubricant and surface conditioner does not have an adverse effect on the adhesion of labels printed on the outside surface as well as of lacquers sprayed on the inside surface of the cans.

Uncleaned aluminum cans obtained from an industrial can manufacturer were washed clean with an alkaline cleaner available from the Parker Amchem Division, Henkel Corporation, Madison Heights, Mich., employing that company's Ridoline.RTM. 3060/306 process. The cans were washed in a laboratory Miniwasher processing 14 cans at a time. The cans were treated with different amounts of lubricant and surface conditioner in the final rinse stage of the washer and then dried in an oven. The lubricant and surface conditioner comprised about a 10% active concentrate of polyoxyethylated isostearate, an ethoxylated nonionic surfactant, available under the tradename Ethox.TM. M1-14 from Ethox Chemicals, Inc., Greenville, S.C. The treated cans were returned to the can manufacturer for line speed and printing quality evaluations. The printed cans were divided into two groups, each consisting of 4 to 6 cans. All were subjected for 20 minutes to one of the following adhesion test solutions:

Test Solution A: 1% Joy.RTM. (a commercial liquid dishwashing detergent, Procter and Gamble Co.) solution in 3:1 deionized water:tap water at a temperature of 180.degree. F.

Test Solution B: 1% Joy.RTM. detergent solution in deionized water at a temperature of 212.degree. F.

After removing the printed cans from the adhesion test solution, each can was cross-hatched using a sharp metal object to expose lines of aluminum which showed through the paint or lacquer, and tested for paint adhesion. This test included applying Scotche transparent tape No. 610 firmly over the cross-hatched area and then drawing the tape back against itself with a rapid pulling motion such that the tape was pulled away from the cross-hatched area. The results of the test were rated as follows: 10, perfect, when the tape did not peel any paint from the surface; 8, acceptable; and 0, total failure. The cans were visually examined for any print or lacquer pick-off signs.

In addition, the cans were evaluated for their coefficient of static friction using a laboratory static friction tester. This device measures the static friction associated with the surface characteristics of aluminum cans. This is done by using a ramp which is raised through an arc of 90.degree. by using a constant speed motor, a spool and a cable attached to the free swinging end of the ramp. A cradle attached to the bottom of the ramp is used to hold 2 cans in horizontal position approximately 0.5 inches apart with the domes facing the fixed end of the ramp. A third can is laid upon the 2 cans with the dome facing the free swinging end of the ramp, and the edges of all 3 cans are aligned so that they are even with each other.

As the ramp begins to move through its arc, a timer is automatically actuated. When the ramp reaches the angle at which the third can slides freely from the 2 lower cans, a photoelectric switch shuts off the timer. It is this time, recorded in seconds, which is commonly referred to as "slip time". The coefficient of static friction is equal to the tangent of the angle swept by the ramp at the time the can begins to move.

The average values for the adhesion test and coefficient of static friction evaluation results are summarized in Table 1 which follows:

TABLE 1______________________________________Lubricant andSurface Adhesion Evaluation Conditioner Test Coefficient ofTest Concentrate Solu- StaticNo. (%/vol.) tion OSW ISW ID Friction______________________________________1 Control (no -- -- -- -- 1.42 treatment)2 0.1 B 10 10 10 0.943 0.25 A 10 10 10 --4 0.5 B 9.5* 10 10 0.805 0.75 A 10 10 10 0.636 1.0 B 10 10 10 0.647 2.0 A 10 10 10 0.568 5.0 B 10 10 10 0.559 10.0 A 9.8* 10 10 0.56______________________________________ *Little pickoff was visually noticed on the outside walls, mainly at the contact marks.

In Table 1, "OSW" stands for outside sidewall, "ISW" stands for inside sidewall, and "lD" stands for inside dome.

In brief, it was found that the lubricant and surface conditioner forming composition as applied to the cleaned aluminum cans provided improved mobility to the cans even at very low active ingredient concentrations, and it had no adverse effect on either adhesion of label print or internal lacquer tested even at 20 to 100 times the required use concentration to reduce the coefficient of static friction of the cans.

EXAMPLE II

This example illustrates the use of the aluminum can lubricant and surface conditioner of Example 1 in an industrial can manufacturing facility when passing cans through a printing station at the rate of 1260 cans per minute.

Aluminum can production was washed with an acidic cleaner (Ridoline.RTM. 125 CO, available from the Parker Amchem Division, Henkel Corporation, Madison Heights, Mich.), and then treated with a non-chromate conversion coating (Alodine.RTM. 404, also available from the Parker Amchem Division, Henkel Corporation, Madison Heights, Mich.). The aluminum can production was then tested for "slip" and the exterior of the cans were found to have a static coefficient of friction of about 1.63. During processing of these cans through a printer station, the cans could be run through the printer station at the rate of 1150 to 1200 cans per minute without excessive "trips", i.e., improperly loaded can events. In such case, the cans are not properly loaded on the mandrel where they are printed. Each "trip" causes a loss of cans which have to be discarded because they are not acceptable for final stage processing.

About 1 ml/liter of aluminum can lubricant and surface conditioner was added to the deionized rinse water system of the can washer, which provided a reduction of the static coefficient of friction on the exterior of the cans to a value of 1.46 or a reduction of about 11 percent from their original value. After passing the cans through the printer, it was found that the adhesion of both the interior and exterior coatings were unaffected by the lubricant and surface conditioner. In addition, the printer speed could be increased to its mechanical limit of 1250 to 1260 cans per minute without new problems.

In similar fashion, by increasing the concentration of the aluminum can lubricant and surface conditioner forming composition in the deionized rinse water system, it was possible to reduce the coefficient of static friction of the cans by 20 percent without adversely affecting the adhesion of the interior and exterior coatings of the cans. Further, it was possible to maintain the printer speed continuously at 1250 cans per minute for a 24-hour test period.

EXAMPLE III

This example illustrates the use of other materials as the basic component for the aluminum can lubricant and surface conditioner.

Aluminum cans were cleaned with an alkaline cleaner solution having a pH of about 12 at about 105.degree. F. for about 35 seconds. The cans were rinsed, and then treated with three different lubricant and surface conditioners comprising various phosphate ester solutions. Phosphate ester solution 1 comprised a phosphate acid ester (available under the tradename Gafac.RTM. PE 510 from GAF Corporation, Wayne, N.J.) at a concentration of 0.5 g/l. Phosphate ester solution 2 comprised an ethoxylated alkyl alcohol phosphate ester (available under the tradename Ethfac.RTM. 161 from Ethox Chemicals, Inc., Greenville, S.C.) at a concentration of 0.5 g/l. Phosphate ester solution 3 comprised an ethoxylated alkyl alcohol phosphate ester (available under the tradename Ethfac.RTM. 136 from Ethox Chemicals, Inc., Greenville, S.C.) at a concentration of 1.5 g/l.

The mobility of the cans in terms of coefficient of static friction was evaluated and found to be as follows:

______________________________________Phosphate Ester Coefficient of StaticSolution pH Friction______________________________________1 3.6 0.472 3.3 0.633 2.6 0.77None -- 1.63______________________________________

The aforementioned phosphate ester solutions all provided an acceptable mobility to aluminum cans, but the cans were completely covered with "waterbreak". It is desired that the cans be free of water-breaks, i.e., have a thin, continuous film of water thereon, because otherwise they contain large water droplets, and the water film is non-uniform and discontinuous. To determine whether such is detrimental to printing of the cans, they were evaluated for adhesion. That is, the decorated cans were cut open and boiled in a 1% liquid dishwashing detergent solution (Joy.RTM.) comprising 3:1 aleionized water:tap water for ten minutes. The cans were then rinsed in deionized water and dried. As in Example I, eight cross-hatched scribe lines were cut into the coating of the cans on the inside and outside sidewalls and the inside dome. The scribe lines were taped over, and then the tape was snapped off. The cans were rated for adhesion values. The average value results are summarized in Table 2.

TABLE 2______________________________________Phosphate ester Adhesion RatingSolution OSW ISW ID______________________________________Control 10 10 101 9.8 6.8 1.02 9.8 10 103 10 10 10______________________________________

In Table 2, "OSW" stands for "outside sidewall", "ISW" stands for "inside sidewall", and "ID" stands for "inside dome".

For the control, it was observed that there was no pick-off (loss of coating adhesion) on either the outside sidewall, the inside sidewall or the inside dome of the cans.

For phosphate ester solution 1, it was observed that there was almost no pick-off on the outside sidewall, substantial pick-off on the inside sidewall, and complete failure on the inside dome of the cans.

For phosphate ester solution 2, it was observed that there was almost no pick-off on the outside sidewall, and no pick-off on the inside sidewall and no pick-off on the inside dome of the cans.

For phosphate ester solution 3, it was observed that there was no pick-off on the outside sidewall, the inside sidewall, and the inside dome of the cans.

EXAMPLE IV

This example illustrates the effect of the lubricant and surface conditioner of this invention on the water draining characteristics of aluminum cans treated therewith.

Aluminum cans were cleaned with acidic cleaner (Ridoline.RTM. 125 CO followed by Alodine.RTM. 404 treatment or Ridoline.RTM. 125 CO only) or with an alkaline cleaner solution (Ridoline.RTM. 3060/306 process ), all the products being available from the Parker Amchem Division, Henkel Corporation, Madison Heights, Mich., and then rinsed with deionized water containing about 0.3% by weight of a lubricant and surface conditioner of this invention. After allowing the thus-rinsed cans to drain for up to 30 seconds, the amount of water remaining on each can was determined. The same test was conducted without the use of the lubricant and surface conditioner. The results are summarized in Table 3.

TABLE 3______________________________________Drain Time, Water Remaining, Grams per CanSeconds With DI Water With 0.3% Conditioner______________________________________ 6 2.4-3.0 not detemiined12 2.1-3.5 2.818 2.2-3.5 2.330 1.8-3.4 2.3______________________________________

It was found that the presence of the lubricant and surface conditioner caused the water to drain more uniformly from the cans, and that the cans remained "water-break" free for a longer time.

EXAMPLE V

This example illustrates the effect of the oven dryoff temperature on the sidewall strength of aluminum cans. This test is a quality control compression test which determines the column strength of the cans by measuring the pressure at which they buckle. The results are summarized in Table 4.

TABLE 4______________________________________Oven Temperature (.degree.F.) Column Strength (PSI)______________________________________440 86.25400 87.75380 88.25360 89.25______________________________________

It can be seen from Table 4 that at an oven drying temperature of 380.degree. F., a 2 psi increase was obtained in the column strength test compared to the value obtained at 440.degree. F. oven temperature.

The higher column strength test results are preferred and often required because the thin walls of the finished cans must withstand the pressure exerted from within after they are filled with a carbonated solution. Otherwise, cans having weak sidewalls will swell and deform or may easily rupture or even explode. It was found that the faster water film drainage resulting from the presence therein of the lubricant and surface conditioner composition of this invention makes it possible to lower the temperature of the drying ovens and in turn obtain higher column strength results. More specifically, in order to obtain adequate drying of the rinsed cans, the cans are allowed to drain briefly before entry into the drying ovens. The time that the cans reside in the drying ovens is typically between 2 and 3 minutes, dependent to some extent on the line speed, oven length, and oven temperature. In order to obtain adequate drying of the cans in this time-frame, the oven temperature is typically about 440.degree. F. However, in a series of tests wherein the rinse water contained about 0.3 % by weight of a lubricant and surface conditioner of this invention, it was found that satisfactory drying of the cans could be obtained wherein the oven temperature was lowered to 400.degree. F., and then to 370.degree. F., and dry cans were still obtained.

EXAMPLES GROUP VI

Uncleaned aluminum cans from an industrial can manufacturer are washed clean in examples Type A with alkaline cleaner available from Parker Amchem Division, Henkel Corporation, Madison Heights, Mich., employing the Ridoline.RTM. 3060/306 process and in Examples Type B with an acidic cleaner, Ridoline.RTM. 125 CO from the same company. Following initial rinsing and before final drying, the cleaned cans are treated with a lubricant and surface conditioner comprised of about a 1% by weight active organic (I) in deionized water as specified in Table 5 below. In a separate set of examples, following initial rinsing and before final drying, the cleaned cans are treated with a reactive lubricant and surface conditioner comprised of about a 1% active organic (I) in deionized water plus about 2 gm/l (0.2wt%) of the inorganic (11) as specified in Table 5, below. In yet another set of examples, following initial rinsing and before final drying, the cleaned cans are treated with a lubricant and surface conditioner comprised of about 1% active organic (I) in deionized water plus about 0.5% by weight of surfactant (111) specified in Table 5, below. In a further set of examples, following initial rinsing and before final drying, the cleaned cans are treated with a reactive lubricant and surface conditioner in deionized water comprised of about 1% active organic (I), about 0.2% inorganic (11), about 0.5% surfactant (111) as specified in Table 5, below.

TABLE 5__________________________________________________________________________ Coefficient ofExample Active Organic (I) static frictionType Trade Name Description Inorganic (II) Surfactant (III) pH after drying__________________________________________________________________________A Emery 657 Caprylic acid Al.sub.2 (SO.sub.4).sub.3 IGEPAL CO-887 2.2 less thad 1.5B Emery 659 Capric acid H.sub.2 ZrF.sub.6 TRITON X-101 2.2 "A Emery 651 Lauric acid FeF.sub.3 NEODOL 25-5-3 2.3 "B Emery 655 Myristic acid SnCl.sub.4 TERGITOL TMN-6 2.3 "A Emersol 143 Palmitic acid 91% Ce(NO.sub.3).sub.4 TRITON DF-16 2.6 "B Emersol 153 NF Stearic acid 92% H.sub.2 TiF.sub.6 TRYCOL 6720 2.6 "A Emersol 871 Isostearic acid H.sub.2 HfF.sub.6 ANTAROX LF-330 2.6 "B Emersol 6313 Oleic acid 75% (NH.sub.4).sub.2 ZrF.sub.6 TRITON H-55 2.6 " NFA Empol 1014 Dimer acid 95% Fe.sub.2 (SO.sub.4).sub.3 TRITON H-66 2.6 "B Emery 1110 Azeleic acid Al(NO.sub.3).sub.3 TRITON QS-44 2.6 "B Ethox MI5 Ethoxylated isostearic TiCl.sub.4 TRYCOL 6720 3.0 " acidA Emulphor VN Polyoxyethylated oleic CeI.sub.3 SURFONIC LF-17 3.0 " 430 acidB Ethox MO5 Polyoxyethylated oleic FeF.sub.3 LOMAR D 3.0 " acidA Monamide 150 Lauric alkanolamide FeCl.sub.3 DOWFAX 2A1 2.0 " LWB Monamide 150 Myristic alkanolamide FeBr.sub.3 DYASULF 9268-A 3.0 " MWA Monamide 150 Isostearic alkanolamide H.sub.2 ZrF.sub.6 DYASULF C-70 4.0 " ISB Monamide 718 Stearic alkanolamide H.sub.2 TiF.sub.6 IGEPAL CO-887 5.0 "A Gafac BH 650 Aliphatic phosphate Fe(NO.sub.3).sub.3 POLYTERGENT SLF- 2.0 " ester, acid form 18B Ethox PP16 Aromatic phosphate (NH.sub.4).sub.2 ZrF.sub.6 PLURONIC L-61 3.0 " esterA Gafac BL 750 Aliphatic phosphate TaF.sub.5 TETRONIC 701 6.0 " ester, acid formB Gafac PE510 Aromatic phosphate NbF.sub.5 PLURONIC 31R1 5.0 " ester, acid formA Ethfac 142W Aliphatic phosphate H.sub.2 ZrF.sub.6 PLURONIC 150R1 4.0 " esterB Gafac RA 600 Aliphatic phosphate (NH.sub.4).sub.2 MoO.sub.4 APG 300 6.0 " ester, acid formA Armeen Z N-Coco-B-aminobutyric H.sub.2 TiF.sub.6 TRITON CF-21 6.0 " acidB Hamposyl L Lauroyl sarcosine VF.sub.4 TRITON DF-18 5.0 "A Hamposyl C Cocoyl sarcosine FeF.sub.3 TRITON GR-7M 4.0 "B Hamposyl O Oleoyl sarcosine SnCl.sub.4 TRITON H-55 3.0 "A Hamposyl S Stearyl sarcosine Al.sub.2 (SO.sub.4).sub.3 TRITON X-100 2.0 "B Acusol 410N Polyacrylic acid, H.sub.2 ZrF.sub.6 TRITON X-120 4.0 " sodium salt,A Neodol 91-2.5 C.sub.9 -C.sub.11 carbons/2.5 H.sub.2 ZrF.sub.6 IGEPAL CO-430 6.0 " ethoxylatesB Neodol 25-12 C.sub.12 -C.sub.15 carbons/12 FeF.sub.3 IGEPAL CO-530 5.0 " ethoxylatesA Neodol 45-7 C.sub.14 -C.sub.15 carbons/7 Ce(NO.sub.3).sub.3 IGEPAL CO-710 4.0 " ethoxylatesB Triton GR-5M Dioctylsulfo-succinate Al(NO.sub.3).sub.3 TRYCOL 5882 6.0 "A Avanel S 70 Sodium alkylether VOSO.sub.4 TRYCOL 5887 5.0 " sulfonateB Igepon TC-42 Sodium N-coconut and VF.sub.5 TRYCOL 5964 4.0 " N-methyl taurateA Igepon TK-32 Sodium N-methyl-N-tall VF.sub.3 IGEPAL CO-887 3.0 " oil acid taurateB Neodol 25-3A Sulfonated linear (NH.sub.4).sub.2 WO.sub.4 IGEPAL CO-630 3.0 " alcohol, ammonium saltA Aromox C/12 Bis(2-hydroxyethyl) (NH.sub.4).sub.2 ZrF.sub.6 NEODOL 25-3 3.0 " cocamine oxideB Aromox DMC Dimethylcocamine FeF.sub.3 NEODOL 25-35 3.0 " oxideA Ethoquad 0/25 Oleyl [POE(15)] Fe.sub.2 (SO.sub.4).sub.3 NEODOL 25-9 2.0 " ammonium chlorideB Ethoquad C/12 Cocomethyl [POE(2)] Al.sub.2 (SO.sub.4).sub.3 NEODOL 91-25 3.0 " ammonium chlorideA Ethoquad 18/5 Octadecyl [POE(15)] Sn(SO.sub.4) TRITON Q5-15 3.0 " ammonium chlorideB Propoquad T/12 Tallowalkyl-methyl-bis- Ce.sub.2 (SO.sub.4).sub.3 TRITON DF-12 2.0 " (2-hydroxy-2- methylethyl) ammonium methyl sulfateA Ethfac 136 Phosphate ester H.sub.2 ZrF.sub.6 IGEPAL 10-887 2.3 "B Ethox 2684 Phosphate ester H.sub.2 ZrF.sub.6 IGEPAL CO-887 2.7 "A Trylox 5922 Ethoxylated H.sub.2 ZrF.sub.6 IGEPAL CO-887 2.3 " hydrogenated castor oilB Trylox 5921 Ethoxylated H.sub.2 TiF.sub.6 IGEPAL CO-887 2.7 " hydrogenated castor oilA Trylox 5925 Ethoxylated H.sub.2 ZrF.sub.6 TRITON H-66 2.7 " hydrogenated castor oil__________________________________________________________________________

EXAMPLE AND COMPARISON EXAMPLE GROUP VII

Two different surfactant combinations were prepared. The first consisted of SURFONIC.TM. LF-17 and TRITON.TM. N-101 in a ratio of 111:156. The second consisted of EMULSOGEN.TM. TP-2144, TRYCOL.TM. LF-1, and ANTAROX LF-330 in a ratio of 201:64.5:64.5. All of these tradenamed surfactants are alkyl polyethers, except for TRITON.TM., which is a nonyl phenol ethoxylate, and EMULSOGEN.TM. TP-2144, which is ethoxylated rosin and therefore contains a phenanthrene ring structure.

About 0.2% of each surfactant combination was added to separate batches of aqueous sulfuric and hydrofluoric acids in the amounts used in conventional acid cleaner for aluminum cans, and these acid-surfactant combinations were used as the base treatment liquid for Stage 2 as defined in Table A above. In order to simulate the build-up of lubricant and aluminum containing species that would occur in normal extended use of such a cleaner for processing large volumes of aluminum cans, there were also added to these cleaning compositions (i) 2 g/L of a lubricant mixture consisting of 30 parts of DTI.TM. 5600 M3 cupper lubricant, 37 parts of DTI.TM. 5600 WB coolant, and 33 parts of Mobil.TM. 629 hydraulic lubricant (the products including the letters "DTI" in their designations above are commercially available from Diversified Technology Inc., San Antonio, Tex., USA) and (ii) sufficient sodium aluminate to correspond to 1980 parts per million stoichiometric equivalent of aluminum. For further simulation of extended operations, Stage 3 as defined in Table A contained 5% by volume of the cleaner solution in tap water as its treatment liquid, and, in some of the experiments, Stage 4 as defined in Table A, in which the treatment liquid was primarily FIXODINE.RTM. 500, was "contaminated" with 0.25 or 1.0% of the cleaner bath, while in other experiments, the Stage 4 treatment liquid was left free from any cleaner bath. (It has been determined by extensive experience that at equilibrium a treatment liquid which is routinely overflowed by addition of less contaminated solution will contain about 5% by volume of the treatment liquid from the previous process stage in addition to its nominal, deliberately added constituents. Stages and 3 treatment liquids are normally routinely overflowed, while Stage 4 treatment liquid normally is not. Therefore, Stage 4 treatment liquid can become even more contaminated than would be expected from carry-over of 5% of the Stage 3 treatment liquid, which would correspond to a content of 0.25% of the Stage 2 treatment liquid.)

In all these experiments, it was observed that the Stage 4 bath developed sludge when the acid cleaning solution containing the second surfactant combination were used, but remained free from sludge when the acid cleaning solution containing the first surfactant combination was used.

EXAMPLE AND COMPARISON EXAMPLE GROUP VIII

These examples and comparison examples were performed on an actual commercial cleaning line, in a plant where the primary materials to be cleaned were DTI.TM. 5600 M3 cupper lubricant, DTI.TM. 5600 WB coolant, and Mobil.TM. 629 hydraulic lubricant. The cleaner used as Stage 2 in the preferred example according to the invention for this group consisted when fresh of 450 parts of aqueous sulfuric acid with a density of 66.degree. Baume, 93 parts of TRITON.TM. DF-16 (commercially available from Union Carbide Corp., reported to have an HLB value of 11.6 and to consist of ethoxylated and then terminally propoxylated linear alcohol molecules with from 8 to 10 carbon atoms in the alcohol residue), 7 parts of PLURAFAC.TM. D-25 (commercially available from BASF Corp., reported to have an HLB value of 10.0 and to consist of molecules of the same type as described above for TRITON.TM. DF-16, except that there are from 10 to 16 carbon atoms in the alcohol residue), and 450 parts of water. The Stage 4 treatment liquid when fresh was FIXODINE.RTM. 500.

These treatment liquids were operated in actual cleaning, with conventional overflowing and replenishment of the various treatment liquids, of more than 1400 aluminum beverage cans per hour for about seven months of continuous operation (except for possible occasional brief line stoppages necessitated by equipment malfunctions or routine maintenance; these are believed not to total more than an average of three days per month). The Stage 2 treatment liquid was maintained at 140.+-.2.degree. F. and the Stage 4 treatment liquid was maintained at110.+-.1.degree. F.

During this operation, at intervals the concentrations of free acid and "Reaction Product" in the Stage 2 treatment liquid were measured as described in Parker Amchem Technical Process Bulletin No. 971, Revision of Apr. 19, 1989, and the concentrations of free acid and "Reaction Product" for the Stage 4 treatment liquid were measured as described in Parker Amchem Technical Process Bulletin No. 1373, Revision of Sep. 22, 1994. The concentrations of dissolved aluminum in parts per million in the Stage 2 and Stage 4 treatment liquids are known to be within .+-.10% of the value obtained by multiplying the Reaction Product value by 90 for Stage 2 and by 18 for Stage 4. The concentrations of the TRITON.TM. DF-16 (abbreviated below as "DF-16") and PLURAFAC.TM. D-25 (abbreviated as "D-25" below) surfactants were calculated from the free acid values by assuming that all the free acidity came from complete ionization of the sulfuric acid in the fresh Stage 2 treatment liquid and that the surfactants were present in the same ratios to the sulfuric acid as in the fresh Stage 2 treatment liquid. Some of the more pertinent values are shown in Table 6 below. In all these instances, the Stage 4 treatment liquid remained free from any discernible sludge, either in suspension in the liquid or atop the foam layer that normally is present during steady state operations in the Stage 4 treatment liquid tank.

TABLE 6______________________________________ Value for Characteristic after the Following Number of Days of Operation:Characteristic 9 71 105 169 204 224______________________________________For Stage 2:Points of 16 14 14 14 14 14Free Acidppm of 1080 990 900 1260 990 990DissolvedAl.sup.+3g/L of DF-16 1.74 1.52 1.52 1.52 1.52 1.52g/L of D-25 0.13 0.11 0.11 0.11 0.11 0.11For Stage 4:pH 2.6 2.7 2.7 2.6 2.6 2.6Points of n.m. 1.0 1.0 1.2 1.5 1.5Free Acidppm of n.m. 252 72 284 306 306DissolvedAl.sup.+3% of CansThat WereWater-Break-Free afterStage 6:On Exterior 100 100 100 100 100 100On Interior 90 100 100 100 100 100______________________________________

In contrast to this, in an otherwise similar production operation in which the Stage 2 treatment liquid contained a surfactant based on ethoxylated rosin acids including a phenanthrene ring structure, solid sludge was observed to accumulate atop the foam layer in the Stage 4 treatment liquid tank. From there, the sludge was occasionally dispersed into various other treatment solutions in the process line and when so dispersed often transferred to the surfaces of the treated cans, causing failures of complete coverage of the can surface by later applied lacquer. Such failures of complete coverage require rejection of the cans in question, and they occurred frequently enough that corrective measures were required to maintain the commercial economic viability of the processing operation.

Claims

1. A process comprising steps of:

(I) cleaning an aluminum can with an aqueous acidic cleaning solution comprising a surfactant component and

(II) contacting the aluminum can after step (i) with an aqueous lubricant and surface conditioner forming composition, distinct from said aqueous acidic cleaning solution, said aqueous lubricant and surface conditioner comprising as dissolved, dispersed, or both dissolved and dispersed components therein (i) water-soluble organic material selected from phosphate esters, alcohols, fatty acids including mono-, di-, tri-, and poly-acids; fatty acid derivatives including salts, hydroxy acids, amides, esters, ethers, and derivatives thereof, and mixtures thereof, and (ii) at least one of the elements selected from zirconium, titanium, cerium, aluminum, iron, tin, vanadium, tantalum, niobium, molybdenum, tungsten, and hafnium in metallic or ionic form.

wherein the improvement comprises utilizing an aqueous acid cleaning solution that contains not more than about 0.1% of carbon atoms that are part of phenanthrene rings and an aqueous lubricant and surface conditioner forming composition that contains not more than about 0.01% of carbon atoms that are pad of phenanthrene rings and wherein the surfactant component of the aqueous acid cleaning solution consists essentially of:

(A) a component of nonionic surfactants selected from the group consisting of surfactants corresponding to general chemical formula (I): ##STR2## where a is 0 or 1; R represents an alkyl moiety that may be branched or unbranched and saturated or unsaturated but does not include any aryl group and the sum of a plus the number of carbon atoms in R is from 10-22; n is an integer from 2 to 4 that may be different from one C.sub.n H.sub.2n O group to another in the same molecule; and b is an integer, the value or values of b being selected so that the hydrophile-lipophile balance ("HLB") of the total component is from about 8 to about 20; and

(B) a component of nonionic surfactants selected from the group consisting of surfactants corresponding to the chemical formula R'-.phi.-(C.sub.n H.sub.2n O).sub.c H, where R' represents an alkyl moiety that may be branched or unbranched and saturated or unsaturated but does not include any aryl group and that has from about 4 to about 16 carbon atoms; .phi. represents a phenylene group; n has the same meaning as for formula (I) above; and c is an integer, the value or values of c being selected so that the HLB of the total component is from about 9 to about 21.

2. A process according to claim 1, wherein the sum of a plus the number of carbon atoms in R is from 12 to 20; n is 2 or 3; the value or values of b are selected so that the HLB of component (A) is from about 10 to about 18; R' has from 6-14 carbon atoms; the value or values of c are selected so that the HLB of component (B) is from about 10.6 to about 19; and the ratio of component (A) to component (B) is from about 0.1 to about 10.

3. A process according to claim 2, wherein the value or values of b are selected so that the HLB of component (A) is from about 10.5 to about 16; the value or values of c are selected so that the HLB of component (B) is from about 11.2 to about 15; and the ratio of component (A) to component (B) is from about 0.2 to about 5.

4. A process according to claim 3, wherein the value or values of b are selected so that the HLB of component (A) is from about 11.0 to about 15; the value or values of c are selected so that the HLB of component (B) is from about 11.7 to about 14.7; and the ratio of component (A) to component (B) is from about 0.3 to about 4.

5. A process according to claim 4, wherein the value or values of b are selected so that the HLB of component (A) is from about 11.3 to about 15; the value or values of c are selected so that the HLB of component (B) is from about 12.2 to about 14.5; and the ratio of component (A) to component (B) is from about 0.4 to about 3.

6. A process according to claim 5, wherein the value or values of b are selected so that the HLB of component (A) is from about 11.5 to about 14; R' has from 8-10 carbon atoms; the value or values of c are selected so that the HLB of component (B) is from about 12.5 to about 14.3; and the ratio of component (A) to component (B) is from about 0.5 to about 2.

7. A process according to claim 6, wherein the sum of a plus the number of carbon atoms in R is from 14 to 18; the value or values of b are selected so that the HLB of component (A) is from about 11.7 to about 13.7; the value or values of c are selected so that the HLB of component (B) is from about 12.7 to about 14.1; and the ratio of component (A) to component (B) is from about 0.5 to about 1.5.

8. A process according to claim 7, wherein the value or values of b are selected so that the HLB of component (A) is from about 11.8 to about 13.5; the value or values of c are selected so that the HLB of component (B) is from about 12.9 to about 13.9; and the ratio of component (A) to component (B) is from about 0.55 to about 1.2.

9. A process according to claim 8, wherein the value or values of b are selected so that the HLB of component (A) is from about 11.9 to about 13.3; the value or values of c are selected so that the HLB of component (B) is from about 13.0 to about 13.8; and the ratio of component (A) to component (B) is from about 0.60 to about 1.0.

10. A process according to claim 9, wherein the value or values of b are selected so that the HLB of component (A) is from about 12.0 to about 13.1; the value or values of c are selected so that the HLB of component (B) is from about 13.1 to about 13.7; and the ratio of component (A) to component (B) is from about 0.62 to about 0.9.

11. A process according to claim 10, wherein the value or values of b are selected so that the HLB of component (A) is from about 12.1 to about 12.9; the value or values of c are selected so that the HLB of component (B) is from about 13.2 to about 13.7; and the ratio of component (A) to component (B) is from about 0.64 to about 0.85.

12. A process according to claim 11, wherein the value or values of b are selected so that the HLB of component (A) is from about 12.1 to about 12.8; the value or values of c are selected so that the HLB of component (B) is from about 13.3 to about 13.6; and the ratio of component (A) to component (B) is from about 0.66 to about 0.83.

13. A process according to claim 12, wherein the value or values of b are selected so that the HLB of component (A) is from about 12.1 to about 12.7 and the ratio of component (A) to component (B) is from about 0.67 to about 0.80.

14. A process according to claim 14, wherein the value or values of b are selected so that the HLB of component (A) is from about 12.1 to about 12.6 and the ratio of component (A) to component (B) is from about 0.68 to about 0.79.

15. A process according to claim 14, wherein the value or values of b are selected so that the HLB of component (A) is from about 12.1 to about 12.5 and the ratio of component (A) to component (B) is from about 0.69 to about 0.78.

16. A process according to claim 15, wherein R' has 9 carbon atoms; the value or values of b are selected so that the HLB of component (A) is from about 12.1 to about 12.4; and the ratio of component (A) to component (B) is from about 0.70 to about 0.77.

17. A process according to claim 16, wherein the value or values of b are selected so that the HLB of component (A) is from about 12.1 to about 12.3 and the ratio of component (A) to component (B) is from about 0.71 to about 0.76.

18. A process according to claim 17, wherein the ratio of component (A) to component (B) is from about 0.71 to about 0.76

19. A process according to claim 18, wherein the ratio of component (A) to component (B) is from about 0.71 to about 0.73.