Classifications

• • C—CHEMISTRY; METALLURGY
  • C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
  • C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
  • C11D3/00—Other compounding ingredients of detergent compositions covered in group C11D1/00
  • C11D3/02—Inorganic compounds ; Elemental compounds
  • C11D3/04—Water-soluble compounds
• • C—CHEMISTRY; METALLURGY
  • C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
  • C23F—NON-MECHANICAL REMOVAL OF METALLIC MATERIAL FROM SURFACE; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL; MULTI-STEP PROCESSES FOR SURFACE TREATMENT OF METALLIC MATERIAL INVOLVING AT LEAST ONE PROCESS PROVIDED FOR IN CLASS C23 AND AT LEAST ONE PROCESS COVERED BY SUBCLASS C21D OR C22F OR CLASS C25
  • C23F1/00—Etching metallic material by chemical means
  • C23F1/10—Etching compositions
  • C23F1/14—Aqueous compositions
  • C23F1/16—Acidic compositions
  • C23F1/20—Acidic compositions for etching aluminium or alloys thereof
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
  • B65D—CONTAINERS FOR STORAGE OR TRANSPORT OF ARTICLES OR MATERIALS, e.g. BAGS, BARRELS, BOTTLES, BOXES, CANS, CARTONS, CRATES, DRUMS, JARS, TANKS, HOPPERS, FORWARDING CONTAINERS; ACCESSORIES, CLOSURES, OR FITTINGS THEREFOR; PACKAGING ELEMENTS; PACKAGES
  • B65D1/00—Containers having bodies formed in one piece, e.g. by casting metallic material, by moulding plastics, by blowing vitreous material, by throwing ceramic material, by moulding pulped fibrous material, by deep-drawing operations performed on sheet material
  • B65D1/12—Cans, casks, barrels, or drums
• • C—CHEMISTRY; METALLURGY
  • C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
  • C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
  • C11D3/00—Other compounding ingredients of detergent compositions covered in group C11D1/00
  • C11D3/16—Organic compounds
  • C11D3/20—Organic compounds containing oxygen
• • C—CHEMISTRY; METALLURGY
  • C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
  • C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
  • C11D7/00—Compositions of detergents based essentially on non-surface-active compounds
  • C11D7/02—Inorganic compounds
  • C11D7/04—Water-soluble compounds
• • C—CHEMISTRY; METALLURGY
  • C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
  • C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
  • C11D7/00—Compositions of detergents based essentially on non-surface-active compounds
  • C11D7/22—Organic compounds
  • C11D7/26—Organic compounds containing oxygen
• • C—CHEMISTRY; METALLURGY
  • C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
  • C23G—CLEANING OR DE-GREASING OF METALLIC MATERIAL BY CHEMICAL METHODS OTHER THAN ELECTROLYSIS
  • C23G1/00—Cleaning or pickling metallic material with solutions or molten salts
• • C—CHEMISTRY; METALLURGY
  • C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
  • C23G—CLEANING OR DE-GREASING OF METALLIC MATERIAL BY CHEMICAL METHODS OTHER THAN ELECTROLYSIS
  • C23G1/00—Cleaning or pickling metallic material with solutions or molten salts
  • C23G1/02—Cleaning or pickling metallic material with solutions or molten salts with acid solutions
  • C23G1/12—Light metals
  • C23G1/125—Light metals aluminium
• • C—CHEMISTRY; METALLURGY
  • C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
  • C23G—CLEANING OR DE-GREASING OF METALLIC MATERIAL BY CHEMICAL METHODS OTHER THAN ELECTROLYSIS
  • C23G1/00—Cleaning or pickling metallic material with solutions or molten salts
  • C23G1/14—Cleaning or pickling metallic material with solutions or molten salts with alkaline solutions
  • C23G1/22—Light metals
• • C—CHEMISTRY; METALLURGY
  • C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
  • C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
  • C11D2111/00—Cleaning compositions characterised by the objects to be cleaned; Cleaning compositions characterised by non-standard cleaning or washing processes
  • C11D2111/10—Objects to be cleaned
  • C11D2111/14—Hard surfaces
  • C11D2111/16—Metals

Definitions

• the present invention relates to a method of treating the surface of an aluminum can.
• aluminium cans such as beverage cans made of aluminum or an aluminium alloy are manufactured by a drawing process called the drawing and ironing process (hereafter referred to as the DI process).
• Aluminum powder hereinafter referred to as smut
• smut Aluminum powder generated by scraping upon drawing and lubricating oil adhere to the surface of an aluminum cans which are manufactured by the DI process.
• aluminum cans are subjected to chemical conversion treatment and paint treatment.
• an oxide film formed on the surface of an aluminum can needs to be removed by etching after completely removing smut and lubricating oil adhering on the surface of the aluminum can before chemical conversion.
• an acidic surface treatment liquid (hereinafter may be referred to as an acid treatment liquid) is commonly used, with which the surface of the aluminum can be moderately etched.
• an acid treatment liquid containing trivalent iron ions in which pH is adjusted to 2 or less with sulfuric acid or nitric acid (for example, see Patent Documents 1 and 2).
• a method of treating the surface of an aluminum can with an acid treatment liquid containing organic sulfonic acid, trivalent iron ions and an inorganic acid such as sulfuric acid and nitric acid for example, see Patent Document 3).
• Patent Document 1 Japanese Examined Patent Application Publication No. H03-50838
• Patent Document 2 Japanese Unexamined Patent Application, Publication No. 2000-104185
• Patent Document 3 Japanese Unexamined Patent Application, Publication No. 2007-197775
• Patent Document 4 Japanese Unexamined Patent Application, Publication No. 2003-119570
• Patent Document 5 Japanese Unexamined Patent Application, Publication No. 2004-18992
• Patent Document 6 Japanese Unexamined Patent Application, Publication No. 2008-127625
• a chemical film or a paint coating film may not be uniformly formed on the surface of the aluminum can, which in turn reduces the corrosion resistance of the aluminum can.
• the amount of etching could be increased by increasing a temperature at which treatment is performed with an acid treatment liquid (for example, to 70° C.)
• a temperature at which treatment is performed with an acid treatment liquid for example, to 70° C.
• Patent Document 3 discloses that a temperature at which treatment is performed with an acid treatment liquid can be decreased by treating the surface of an aluminum can with an acid treatment liquid containing organic sulfonic acid. However, even in a case where the acid treatment liquid containing organic sulfonic acid is used, etching may not proceed sufficiently at a low temperature.
• acid wash is performed at a relatively low temperature (for example, at 50° C.) in the surface preparation of an aluminum for can tops disclosed in Patent Documents 4 to 6.
• a substrate surface is etched by treatment with an alkaline solution performed before the acid wash.
• the acid wash in this case appears to be intended for removing magnesium segregated on an aluminum surface and for neutralizing an aluminum surface alkalinized by the treatment with an alkaline solution before the acid wash.
• the purposes are completely different for the acid wash in the surface preparation of an aluminum for can tops, and for the treatment of etching a substrate surface with an acid treatment liquid performed in the surface treatment of an aluminum can.
• an aluminum can is treated under the conditions for the surface preparation of an aluminum for can tops, the amount of etching on the surface of an aluminum can would not be controlled, and thus a finishing appearance of the aluminum can may not be controlled. Therefore, the technology for the surface preparation of an aluminum for can tops can not be applied to that for treating the surface of an aluminum can.
• An objective of the present invention is to provide a method of treating the surface of an aluminum can in which an acid treatment liquid with easy handling can be used, and the energy cost is sufficiently low.
• the present invention relates to a method of treating a surface of an aluminum can.
• the method includes: an alkaline treatment step of treating the aluminum can with an alkaline treatment liquid; and an acid treatment step of treating the aluminum can after the alkaline treatment step with an acid treatment liquid, in which the amount of etching in the alkaline treatment step is less than 50 mg/m 2 .
• the alkaline treatment liquid preferably contains at least one selected from the group consisting of sodium ions, potassium ions and ammonium ions.
• the alkaline treatment liquid is at 40 to 70° C., and a treatment time of the aluminum can in the alkaline treatment step is 1 to 30 seconds.
• the alkaline treatment liquid preferably contains at least one selected from the group consisting of an organic acid, a chelating agent, a dispersing agent and a surfactant.
• the acid treatment liquid contains at least one selected from the group consisting of sulfuric acid, nitric acid and phosphoric acid, and contains 0.05 to 4 g/L of trivalent iron ions, and has a pH of 2 or less, and a treatment temperature of the aluminum can in the acid treatment step is 30 to 65° C.
• a treatment time of the aluminum can in the acid treatment step is preferably 10 to 90 seconds.
• the present invention relates to an aluminum can subjected to a surface treatment by the method of treating a surface of an aluminum can.
• the present invention can provide a method of treating the surface of an aluminum can in which an acid treatment liquid with easy handling can be used, and the energy cost is sufficiently low.
• the method of treating the surface of an aluminum can according to the present invention includes an alkaline treatment step and an acid treatment step.
• Aluminum cans to be treated by the surface treatment method according to the present embodiment include those made of a 3000-series alloy and the like.
• an aluminum can is treated with an alkaline treatment liquid.
• the alkaline treatment liquid removes fat and oil components on the surface of an aluminum can. Further, in a case where an aluminum can after the DI process is treated, the alkaline treatment liquid also serves to remove a lubricant.
• the amount of etching on the surface of an aluminum can in the alkaline treatment step is less than 50 mg/m 2 . That is, the surface of an aluminum can hardly etched in the alkaline treatment step. In a case where the amount of etching in the alkaline treatment step is 50 mg/m 2 or more, etching is difficult to be controlled, resulting in whitening of the surface of an aluminum can.
• the amount of etching on the surface of an aluminum can in the alkaline treatment step can be calculated by measuring the mass of the aluminum can before and after the alkaline treatment step with a precision balance, and dividing the decrement in the mass of the aluminum can before and after the alkaline treatment step by the surface area of the aluminum can.
• the amount of etching on the surface of an aluminum can of less than 50 mg/m 2 in the alkaline treatment step, it is necessary to control the pH of an alkaline treatment liquid, the concentration of an alkaline substance in the alkaline treatment liquid, the treatment time in the alkaline treatment step and the treatment temperature in the alkaline treatment step. More specifically, the amount of etching on the surface of an aluminum can be increased by increasing the concentration of an alkaline substance in the alkaline treatment liquid, i.e., increasing the pH of the alkaline treatment liquid, whereas the amount of etching can be decreased by decreasing it.
• the amount of etching on the surface of an aluminum can also be increased by increasing the treatment time in the alkaline treatment step or increasing the temperature of alkaline treatment whereas the amount of etching can be decreased by decreasing the treatment time or the treatment temperature. Note that all of these factors may not necessarily need to be adjusted, and an amount of etching on the surface of an aluminum can of less than 50 mg/m 2 may be achieved by adjusting only some of them.
• the alkaline treatment liquid preferably has a pH of 9 to 14.
• a pH of the alkaline treatment liquid of 9 to 14 can allow a hydroxide film to form on the surface of an aluminum can.
• the hydroxide film formed on the surface of an aluminum can in the alkaline treatment step will be dissolved with an acid treatment liquid in the acid treatment step described below.
• the pH of the alkaline treatment liquid is more preferably 10.0 to 13.0.
• the alkaline treatment liquid preferably contains at least one selected from the group consisting of sodium ions, potassium ions and ammonium ions. These ions contained in the alkaline treatment liquid can form a hydroxide film effectively on the surface of an aluminum can.
• Sources of sodium ions, potassium ions and ammonium ions include inorganic substances such as sodium hydroxide, potassium hydroxide, sodium carbonate, sodium hydrogen carbonate and ammonium hydrogen carbonate; and organic substances such as sodium, potassium and ammonium salts of organic acids such as gluconic acid and citric acid. These compounds may be used in combination of two or more.
• the alkaline treatment liquid is preferably an aqueous solution containing sodium hydroxide.
• a hydroxide film can be formed more effectively on the surface of an aluminum can.
• the concentration of an alkaline substance such as sodium hydroxide in the alkaline treatment liquid is preferably 0.01 to 10 g/L.
• concentration of an alkaline substance in the alkaline treatment liquid is less than 0.01 g/L, a hydroxide film tends not to be easily formed on the surface of an aluminum can.
• whitening may occur due to excessive etching of the surface of an aluminum can.
• the alkaline treatment liquid preferably contains at least one selected from the group consisting of organic acids, chelating agents, dispersing agents and surfactants.
• the alkaline treatment liquid contains an organic acid, a chelating agent, a dispersing agent or a surfactant, smut on the surface of an aluminum can may efficiently be removed, and the formation of a hydroxide film can be promoted even if the alkaline treatment step is performed under mild conditions (for example, at low temperature, for short time).
• Organic acids to be contained in the alkaline treatment liquid can include gluconic acid, citric acid, oxalic acid, malic acid, tartaric acid, sorbic acid, succinic acid and the like, and alkali metal salts such as sodium salts and potassium salts thereof.
• the alkaline treatment liquid more preferably contains at least one selected from the group consisting of gluconic acid, citric acid, oxalic acid, malic acid and tartaric acid.
• Chelating agents to be contained in the alkaline treatment liquid can include aminocarboxylic acid-based chelating agents, phosphonic acid-based chelating agents and condensed phosphates. Specifically, they include ethylenediaminetetraacetic acid (EDTA), sodium 1-hydroxyethylidene-1,1-diphosphonate (HEDP), trisodium nitrilotriacetate (NTA), sodium tripolyphosphate (STPP) and the like. Among these, the alkaline treatment liquid more preferably contains at least one of ethylenediaminetetraacetic acid (EDTA) and sodium 1-hydroxyethylidene-1,1-diphosphonate (HEDP).
• EDTA ethylenediaminetetraacetic acid
• HEDP sodium 1-hydroxyethylidene-1,1-diphosphonate
• HEDP 1-hydroxyethylidene-1,1-diphosphonate
• Dispersing agents to be contained in the alkaline treatment liquid can include acrylic acid-maleic acid copolymer and a sodium salt thereof, polycarboxylic acid, polyethylene glycol and the like.
• the alkaline treatment liquid more preferably contains acrylic acid-maleic acid copolymer.
• nonionic, cationic, anionic and zwitterionic surfactants can be used.
• nonionic systems are particularly preferred.
• hydrocarbon derivatives, abietic acid derivatives, alcohol ethoxylate, denatured polyethoxylated alcohol and the like are preferably used.
• the alkaline treatment liquid more preferably contains at least one selected from the group consisting of organic acids, chelating agents and dispersing agents; and a surfactant. That is, preferred combinations of additives to be contained in the alkaline treatment liquid are combinations of at least one selected from the group consisting of organic acids, chelating agents and dispersing agents; and surfactants.
• both smut and lubricating oil on the surface of an aluminum can effectively be removed to further promote the formation of a hydroxide film even if the alkaline treatment step is performed under mild conditions (for example, at low temperature, for a short time) as described above. Therefore, in a case where the alkaline treatment liquid contains at least one selected from the group consisting of organic acids, chelating agents and dispersing agents; and a surfactant, consequently, desmutting of an aluminum can after the surface treatment can be further improved even if the alkaline treatment is performed under mild conditions.
• the treatment time of an aluminum can in the alkaline treatment step is preferably 1 to 30 seconds. In a case where the treatment time of an aluminum can in the alkaline treatment step is shorter than 1 second, a hydroxide film tends not to be easily formed on the surface of the aluminum can. On the other hand, in a case where it is longer than 30 seconds, whitening of the surface of the aluminum can may occur due to excessive etching.
• the treatment time of an aluminum can in the alkaline treatment step is more preferably 3 to 20 seconds.
• the treatment temperature of an aluminum can in the alkaline treatment step (the temperature of the alkaline treatment liquid) is preferably 40 to 70° C. In a case where the treatment temperature of an aluminum can in the alkaline treatment step is lower than 40° C., a hydroxide film tends not to be easily formed on the surface of the aluminum can. On the other hand, in a case where it is higher than 70° C., whitening of the surface of the aluminum can may occur due to excessive etching.
• the treatment temperature of an aluminum can in the alkaline treatment step is more preferably 45 to 60° C.
• Methods of treating an aluminum can in the alkaline treatment step include the spray method and the dipping method.
• Treatment with the aforementioned alkaline treatment liquid may be performed once or multiple times in the alkaline treatment step.
• the treatment conditions for each treatment may be the same or may be altered.
• the aluminum in the acid treatment step, the aluminum can after the alkaline treatment step is treated with an acid treatment liquid.
• a hydroxide film is formed on the surface of an aluminum can without being passivated in the aforementioned alkaline treatment step. Since a hydroxide film is easily dissolved in an acid treatment liquid, the surface of an aluminum can be etched with a low-temperature acid treatment liquid in the acid treatment step. If the surface of an aluminum can were treated in the acid treatment step without performing the alkaline treatment step, the surface of the aluminum can would be passivated. Therefore, the temperature of the acid treatment liquid would need to be increased in order to facilitate etching.
• a high treatment temperature of an aluminum can (a high temperature of an acid treatment liquid) in the acid treatment step is not preferred because the energy cost in the surface treatment of an aluminum can is too high. In a case where the alkaline treatment step has been performed before the acid treatment step, the temperature of an acid treatment liquid can be lowered by 5 to 20° C. as compared with the case where the alkaline treatment step has not been performed.
• the acid treatment liquid preferably has a pH of 2 or less.
• pH of the acid treatment liquid is more than 2, etching of the surface of an aluminum can tends to be insufficient.
• the acid treatment liquid preferably contains inorganic acid.
• Inorganic acid will serve as an etching accelerator.
• Specific examples of inorganic acid include sulfuric acid, nitric acid and phosphoric acid, and these inorganic acids may be used alone or in combination. Note that sulfuric acid is more preferably used in view of being free of nitrogen and phosphorus.
• the content of an inorganic acid in the acid treatment liquid is preferably 0.01 to 25 g/L. In a case where the content of an inorganic acid in the acid treatment liquid is less than 0.01 g/L, an etching rate is extremely low. On the other hand, in a case where it is more than 25 g/L, no further improvement is observed for the effect of etching, which is economically disadvantageous.
• the content of an inorganic acid in a more preferred acid treatment liquid is 0.5 to 20 g/L.
• the acid treatment liquid preferably contains oxidized metal ions.
• the etching reaction of aluminum in the acid treatment step includes an anode reaction in which aluminum becomes an aluminum ion (Al 3+ ) and a cathode reaction in which H + in the acid treatment liquid is reduced into 1 ⁇ 2H 2 .
• anode reaction in which the above Fe 3+ is reduced into Fe 2+ occurs simultaneously as the aforementioned reduction of H + , promoting the etching reaction of aluminum.
• the adhesiveness of the metal with a chemical conversion film formed by chemical conversion after the acid treatment step is improved in a case where the acid treatment liquid contains oxidized metal ions.
• oxidized metal ions include metavanadic acid ions (VO 3 ⁇ ), ceric ions (Ce 4+ ), cobalt ions (Co 5+ ), stannic ions (Sn 4+ ) and the like.
• trivalent iron ions (ferric ions: Fe 3+ ) are preferably used as oxidized metal ions.
• Oxidized metal ions are preferably supplied from water-soluble salts such as sulfate or nitrate. Therefore, trivalent iron ions are preferably supplied from ferric sulfate or ferric nitrate.
• ORP oxidation-reduction potential
• an oxidizing agent for controlling ORP may be added as needed or at the beginning to oxidize ferrous ions into ferric ions.
• Oxidizing agents for controlling ORP at this time include hydrogen peroxide (H 2 O 2 ), persulfates (for example, NaS 2 O 8 2 ⁇ ), ozone (O 3 ), cerium compounds (for example, cerium ammonium sulfate: (NH 4 ) 4 Ce(SO 4 ) 4 ), nitrites (for example, NaNO 2 , KNO 2 ) and the like.
• metavanadate may be supplied as needed when metavanadic acid ions are used as oxidized metal ions.
• the content of oxidized metal ions in the acid treatment liquid is preferably 0.05 to 4 g/L.
• the content of oxidized metal ions in the acid treatment liquid is less than 0.05 g/L, the amount of etching is insufficient, deteriorating desmutting properties.
• the content of oxidized metal ions in a more preferred acid treatment liquid is 0.1 to 1 g/L.
• the acid treatment liquid preferably contains a surfactant.
• Surfactants primarily serve to remove fat and oil components and lubricants remained on the surface of an aluminum can. They also serve to prevent removed fat and oil components and lubricant components from being suspended in a cleaning agent. That is, when fat and oil components and lubricant components are suspended in a cleaning agent, they may be re-adsorbed on the surface of an aluminum can. However, this problem can be avoided in a case where the acid treatment liquid contains a surfactant.
• nonionic, cationic, anionic and zwitterionic surfactants can be used as a surfactant.
• nonionic systems are particularly preferred, and for example, ethoxylated alkylphenol systems, hydrocarbon derivatives, abietic acid derivatives, primary ethoxylated alcohols, denatured polyethoxylated alcohols and the like are preferably used.
• the content of a surfactant in the acid treatment liquid is preferably 0.01 to 10 g/L. In a case where the content of a surfactant in the acid treatment liquid is less than 0.01 g/L, detergency, in particular, a degreasing property is decreased. On the other hand, in a case where it is more than 10 g/L, the acid treatment agent may undergo foam formation, resulting in difficult treatment and further imposing a load on wastewater treatment.
• the content of a surfactant in a more preferred acid treatment liquid is 0.1 to 5 g/L.
• the content of organic sulfonic acid in the acid treatment liquid is preferably 0.01 to 25 g/L. In a case where the content of organic sulfone in the acid treatment liquid is less than 0.01 g/L, a sufficient amount of etching may not be obtained. On the other hand, in a case where it is more than g/L, the liquid stability of the acid treatment liquid tends to be decreased. In view of reducing a drain water load, the more preferred content of organic sulfonic acid in the acid treatment liquid is 0.1 to 5 g/L.
• the amount of etching on the surface of an aluminum can in the acid treatment step is 60 to 100 mg/m 2 .
• the amount of etching in the acid treatment step is less than mg/m 2 , etching is insufficient. Therefore, a chemical conversion film and a paint film described below tend not be easily formed on the surface of an aluminum can.
• the amount of etching in the acid treatment step is more than 100 mg/m 2 , etching excessively proceeds. Therefore, whitening may occur on the surface of an aluminum can.
• the amount of etching on the surface of an aluminum can in the acid treatment step can be determined by measuring the mass of the aluminum can before and after the acid treatment step with a precision balance, and dividing the decrement in the mass of the aluminum can before and after the acid treatment step by the surface area of the aluminum can.
• Methods of treating an aluminum can in the acid treatment step include the spray method and the dipping method.
• the treatment time of an aluminum can in the acid treatment step is preferably 10 to 90 seconds. In a case where the treatment time of an aluminum can in the acid treatment step is shorter than 10 seconds, etching on the surface of the aluminum can tends to be insufficient due to the too short treatment time. On the other hand, in a case where it is longer than 90 seconds, the surface of an aluminum can is excessively etched, resulting in a tendency of accelerated aging of an acid treatment agent.
• the treatment time of an aluminum can in the acid treatment step is more preferably 30 to 45 seconds.
• the treatment temperature of an aluminum can in the acid treatment step is preferably 30 to 65° C. In a case where the treatment temperature of an aluminum can in the acid treatment step is lower than 30° C., the treatment temperature tends to be more difficult to be controlled. On the other hand, in a case where it is higher than 65° C., the energy cost tends to be increased.
• the treatment temperature of an aluminum can in the acid treatment step is more preferably 40 to 60° C.
• the aluminum can after the acid treatment step is washed with water according to the conventionally known method, and then subjected to a chemical conversion treatment with a phosphate-based or zircon-based chemical conversion liquid.
• the aluminum can after the chemical conversion treatment is washed with water if necessary, and then subjected to paint treatment.
• Smut and lubricating oil are removed from the aluminum can subjected to the surface treatment by the method of treating the surface of an aluminum can according to the present embodiment. Therefore, a robust chemical conversion film and paint film can be formed.
• an aluminum can prepared was a lidless container having lubricating oil and smut adhered thereon, which was obtained by performing the DI process on a aluminum plate of a 3004 series alloy.
• the resulting material was subjected to a spray treatment at a treatment temperature of 40° C. for 10 seconds using an alkaline treatment liquid adjusted to a pH of 12.5 with sodium hydroxide as an alkaline substance (the alkaline treatment).
• the aluminum can was subjected to a spray treatment at a treatment temperature of 50° C.
• an acid treatment liquid having 1 g/L of ferric ions and 2 g/L of a nonionic surfactant and adjusted to a pH of 1.0 with sulfuric acid as an acidic substance (the acid treatment).
• the source of ferric ions for the acid treatment liquid is ferric sulfate.
• washing was performed with tap water for 15 seconds, and then chemical conversion was further performed (at 40° C., for 12 seconds) with a chemical conversion agent (“Arusafu 450”, Nippon Paint Co., Ltd.) under treatment conditions adjusted so that the amount of Zr in the film was 11 mg/m 2 .
• a chemical conversion agent (“Arusafu 450”, Nippon Paint Co., Ltd.) under treatment conditions adjusted so that the amount of Zr in the film was 11 mg/m 2 .
• spray washing was performed with deionized water for 5 seconds, and dried for 3 minutes at 195° C.
• the same aluminum can as used in Example 1 was subjected to a spray treatment with an alkaline treatment liquid adjusted to a pH shown in Tables 1 and 2 using an alkaline substance shown in Tables 1 and 2 at a treatment temperature and treatment time shown in Tables 1 and (the alkaline treatment).
• the aluminum can after the alkaline treatment was subjected to a spray treatment with an acid treatment liquid containing ferric ions, a nonionic surfactant and, if desired, organic sulfonic acid (HSO 3 —CH 2 CH(OH)CH 2 OH) at concentrations shown in Tables 1 and 2 and adjusted to a pH shown in Tables 1 and 2 at a treatment temperature and treatment time shown in Tables 1 and 2 (the acid treatment).
• an acid treatment liquid containing ferric ions, a nonionic surfactant and, if desired, organic sulfonic acid (HSO 3 —CH 2 CH(OH)CH 2 OH)
• Aluminum cans were treated as described above under the same conditions as in Example 1 except that the conditions were changed as shown in Tables 1 and 2.
• the alkaline treatment step was not performed, but an aluminum can was washed at the same temperature as that of the acid treatment for 10 seconds using a liquid obtained by diluting the acid treatment liquid to be used in the next acid treatment step into a half of the concentration, and then subjected to the acid treatment step.
• Ferric ions were not contained in the acid treatment liquid for Example 23 and Comparative Examples 13, and a surfactant was not contained in the acid treatment liquid for Comparative Examples 3 and 6.
• the alkaline treatment step was not performed, but a spray treatment was performed at a treatment temperature of 60° C. for 60 seconds with an alkaline degreasing liquid containing a surfactant and a chelating agent and adjusted to a pH of 12.5 using sodium hydroxide as an alkaline substance (the alkaline degreasing treatment). Subsequently, the aluminum can after the alkaline treatment was subjected to the acid treatment step performed under the conditions shown in Table 2.
• the same aluminum can as used in Example 1 was subjected to a spray treatment at a treatment temperature and treating time shown in Table 3 with an alkaline treatment liquid containing an organic acid, a chelating agent, a dispersing agent and a surfactant at concentrations shown in Table 3 and adjusted to a pH shown in Table 3 using an alkaline substance shown in Table 3 (the alkaline treatment).
• the aluminum can after the alkaline treatment was subjected to a spray treatment at a treatment temperature and treatment time shown in Table 3 with an acid treatment liquid containing ferric ions and a nonionic surfactant at concentrations shown in Table 3 and adjusted to a pH shown in Table 3 (the acid treatment).
• Aluminum cans were treated as described above under the same conditions as in Example 1 except that the conditions were changed as shown in Table 3. Note that in a case where a surfactant was contained in the alkaline treatment liquid, 2 g/L of a nonionic surfactant was contained. Further, the acrylic acid-maleic acid copolymer used in Example 35 is SOKALAN CP5 from Basf Japan.
• the alkaline treatment step was not performed, but the same aluminum can as used in Example 1 was subjected to a spray treatment at a treatment temperature and treatment time shown in Table 3 with an acidic solution containing 0.5 g/L of citric acid. Then, in the acid treatment step, the aluminum can was subjected to a spray treatment at a treatment temperature and treatment time shown in Table 3 with an acid treatment liquid containing ferric ions and a nonionic surfactant at concentrations shown in Table 3 and adjusted to a pH shown in Table 3.
• the mass of an aluminum can before and after the alkaline treatment step was measured with a precision balance.
• the decrement in the mass of the aluminum can before and after the alkaline treatment step was divided by the surface area of the aluminum can.
• the resulting value was taken as the amount of etching, which was evaluated into the following 2 categories. Results are shown in Tables 1, 2 and 3.
• A less than 50 mg/m 2
• B 50 to 100 mg/m 2
• Transparent adhesive tapes were made adhered on the surfaces of the aluminum cans after the surface treatment obtained from the present Examples, Comparative Examples and Reference Examples. Next, they were removed, and then attached on white mount paper to compare the whiteness of the surfaces of the attached tapes with other parts of the white mount paper. Those in which smut was completely removed without contamination were considered as Good, and evaluated into the following 5 categories depending on the degree of contamination. Results are shown in Tables 1, 2 and 3.
• Appearance evaluation was performed according to the following criteria after immersing the aluminum cans after the surface treatment obtained from the present Examples, Comparative Examples and Reference Examples in boiling water for 30 minutes. Results are shown in Tables 1, 2 and 3.
• the surface of an aluminum can be sufficiently etched when the temperature of the acid treatment is increased even in a case where the acid treatment is performed without performing the alkaline treatment. Therefore, the surface of an aluminum can excellent in the appearance, the water wettability, the degree of desmutting and the resistance to boiling-water blackening (corrosion resistance) can be obtained.
• Example 25 when Example 25 is compared with Reference Example 2, good evaluation results are obtained for Example 25 as well as in Reference Example 2 while the treatment temperature of the acid treatment step is lower by 20° C. than that of Reference Example 2. Therefore, even in a case where the acid treatment liquid contained organic sulfonic acid, it was possible to decrease the temperature of the acid treatment step by 20° C. when the alkaline treatment step was first performed prior to the acid treatment step.
• Example 26 when Example 26 is compared with Reference Example 3, good evaluation results are obtained for Example 26 as well as in Reference Example 3 while the treatment temperature of the acid treatment step is lower by 10° C. than that of Reference Example 1. Therefore, even in a case where the acid treatment liquid contained a large amount of organic sulfonic acid (25 g/L), it was possible to decrease the temperature of the acid treatment step by 10° C. when the alkaline treatment step was first performed prior to the acid treatment step.
• Example 27 desmutting of the surface treated aluminum can was found to be better when an organic acid, a chelating agent, a dispersing agent or a surfactant was contained in the alkaline treatment liquid as compared with the case where these were not contained even though the alkaline treatment step was performed under mild conditions (for short time).
• the above results are likely to be caused because smut on the surface of an aluminum can is efficiently removed in a case where the alkaline treatment liquid contains an organic acid, a chelating agent or a dispersing agent, leading to facilitation in the formation of a hydroxide film.
• the alkaline treatment liquid contains a surfactant
• lubricating oil on the surface of an aluminum is efficiently removed, and this likely leads to facilitation in the formation of a hydroxide film.

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