Process of inhibiting corrosion

Abstract: A process is disclosed for inhibiting corrosion in tin-plated steel aerosol cans which contain aqueous aerosol formulations and a propellant. Compositions such as the isopropylamine, cyclohexylamine, 2-ethylhexylamine and tertiary C₁₂₋₁₄ alkyl primary amine salts of N-acyl sarcosine; morpholine salts of oleic acid, acetic acid, benzoic acid, and N-acyl sarcosine; cyclohexylamine, 2-ethylhexylamine, tertiary C₁₂₋₁₄ alkyl primary amine and tertiary C₁₈₋₂₂ alkyl primary amine salts of benzoic acid are disclosed.

Description: This invention relates to a process of inhibiting corrosion in aerosol products. Many products designed for household, personal, automotive and other types of use are available as aerosol products. Examples of such aerosol products include: personal products such as hair care products (sprays, coloring agents and styling/conditioning mousses), deodorants, antiperspirants, first aid sprays, and colognes; household products such as waxes, polishes, pan sprays, insecticides and room fresheners; automotive products such as cleaners and polishes; industrial products such as cleaners, lubricants and mold release agents; and animal care products such as tick and flea repellants. Although some aerosol products are packaged in glass bottles or aluminum cans or lined steel cans, most formulations are packaged in unlined cans made of tin-plated steel which may corrode during storage or use. While the tin affords some protection against corrosion, the thinness of the coating, imperfections in the surface, wear and tear, and chemical action may ultimately expose the steel to the contents of the can, and allow corrosion to occur. This corrosion can lead to contamination of the aerosol product and ultimately to the rupture of the can, if the corrosion is severe enough. Water based aerosol formulations are being used increasingly to lower the flammability of the aerosol propellant and reduce manufacturing costs. However, the presence of water in an aerosol formulation increases the possibility of corrosion of tin-plated steel cans. Usually a packaged aerosol contains both liquid and vapor phases and corrosion can occur on the interior surface of the can which is in contact with either phase. In addition, corrosion is more likely to occur when more than 80 ppm (parts per million) water is present. For example, in a system that includes dimethyl ether, a propellant and water, corrosion of the can which is in contact with the vapor phase may be aggravated by the fact that relatively large amounts of water vapor are present with the propellant; for example, the vapor phase of a 95/5 wt. % dimethyl ether/water system contains 7,750 ppm water vapor at 70°F (21.1°C). Moreover, the addition of ethanol to a DME/water system will often increase the amount of water vapor in the vapor phase and exacerbate the problem of vapor phase corrosion; a 90/5/5 (wt. %) DME/ethanol/water system will contain 9,100 ppm water vapor at 70°F (21.1°C). Corrosion inhibitors are therefore useful when water-based aerosol formulations are packaged in tin-plated steel cans. However, many commercially available corrosion inhibitors are either ineffective for aerosol systems containing water or they fail to provide adequate protection against both liquid phase and vapor phase corrosion. It often happens that a corrosion inhibitor provides good liquid phase protection but fails to provide effective vapor phase protection. The reverse can also occur. US-A-4 602 958 relates to corrosion inhibitor compositions for tin-plated aerosol cans containing water-based aerosol formulations. Compositions comprising a volatile amine and a tertiary C 12-14 alkyl-ammonium carboxylate are disclosed. US-A-3 337 472 relates to corrosion inhibition of ferrous metals contacted by petroleum fractions. The use of at least two of alkyl-1-(2-hydroxyethylimidazoline), N-tallow-diaminopropane-C 18 -carboxylic acid salts and N-acyl-methylamino acetic acid is suggested. Certain amine salts have been found to be unexpectedly effective as corrosion inhibitors for tin-plated steel aerosol cans. The structures of these amine salts are: (1) Salts of polyamines such as N-tallow-1,3-diaminopropane and oleic acid. (2) Salts of imidazolines such as 1-(2-hydroxyethyl) 2-tall oil-2-imidazoline and oleic acid. The invention relates to a process of inhibiting corrosion in a tin-plated steel aerosol can containing an aqueous aerosol formulation and a propellant comprising contacting the aqueous aerosol formulation, the propellant and an effective amount of between 0.1 and 1 wt. % based on the total weight of the aqueous aerosol formulation and the propellant of a neutral corrosion inhibitor compound selected from salts of N-tallow-1,3-diaminopropane and oleic acid, salts of 1-(2-hydroxyethyl)2-tall oil-2-imidazoline and oleic acid with the interior of a tin-plated steel aerosol can. Even though tin-plated, steel aerosol cans may have steel surfaces which are subject to corrosive attack. The steel may be exposed because the tin plate is applied nonuniformly and/or may have porosity as applied. The seams which connect the sides, bottoms, and dome sections of the aerosol cans together often have unplated surfaces. In addition, the aerosol formulation may cause detinning of the tin-plate and thereby expose the underlying steel surface. It is believed that the subject amine salts prevent corrosion of these exposed steel surfaces and/or detinning of the tin-plate itself by forming protective films in both the vapor and liquid phases. The subject amine salts can be used with a variety of propellants. Because they are essentially neutral compounds with respect to pH, they can be used with propellants such as FC-22 which is readily hydrolyzed at pH values above 8. In addition, the subject amine salts can be used with DME, which is particularly compatible with water. DME can be used either alone or in combination with other well known aerosol propellants such as: monochlorodifluoromethane (FC-22), 1-chloro-1,1-difluoroethane (FC-142b), 1,1-difluoroethane (FC-152a); hydrocarbons such as butane, isobutane and propane; compressed gases such as CO 2 and nitrogen; and mixtures of these propellants. The corrosion inhibitor compositions of this invention can be used in aerosols containing any of these propellants or combinations thereof. The corrosion inhibitor compositions used in the process of this invention can usually be prepared by using commercially available materials. The corrosion inhibitor, the commercial designation and source for various of these compositions are shown later. The effective concentration range of the subject corrosion inhibitor compositions is generally 0.1 to 1 wt. % based on the combined total weight of the propellant(s), the weight of the other ingredients and the corrosion inhibitor. A preferred weight range is 0.25 to 0.5 wt. % of the aerosol formulation. The corrosion inhibitor compositions can be added to the aerosol system in different ways. They can either be added alone or mixed with other ingredients prior to introduction into the aerosol container. If preferred, they can also be combined with the propellant(s) first and subsequently this combination can be added to the aerosol container using well known techniques. This is a particularly convenient way to incorporate the inhibitor into the final aerosol formulation. For example, the subject amine salts are all soluble in DME and DME/FC-22 blends. Such solubility permits the DME or DME-blended propellant to be supplied to the aerosol formulator or loader with the corrosion inhibition composition already present. When combined with the propellant, the amount of corrosion inhibitor composition can be selected to provide the desired 0.1 to 1 wt. % of corrosion inhibitor composition in the final aerosol composition. U.S. Patent 4,315,910 discloses methods for preparing and adding aerosol formulations and propellants to aerosol containers, which is hereby incorporated by reference. The composition of the aqueous aerosol dispersible media which is, in essence, the formulation containing the active ingredients, will, quite naturally, depend upon the use for which the aerosol is designed. Such formulations are well known to persons skilled in the art, and the choice of formulation is not critical to the use of the invention so long as the medium is compatible with the components of the inhibitor composition. The use of the corrosion inhibitors in tin-plated cans with dry-type antiperspirants containing aluminum chlorohydrate is not recommended. Lined cans should be used in these instances. It is common practice in the aerosol industry to evaluate corrosion inhibitors in accelerated aging tests. Thus, corrosion test data developed for aerosol cans of representative product formulations exposed to temperatures of 37.8-48.9°C (100-120°F) have been found, through experience, to correlate well with the shelf-life of commercial products. Thus, 60-day tests a 48.9°C (120°F) which have been conducted for the subject corrosion inhibitors are expected to correlate well with actual product storage in stores, warehouses, etc. Examples Sixty-day corrosion tests at 120°F (48.9°C) were run on the corrosion inhibitors in four aerosol formulations. These formulations were selected as being representative of commercial products, in their chemical compositions. Distilled water was used in each of the formulations because it was readily available in the laboratory. However, similar results would be expected with deionized water which is often used in commercial aerosols. Formulations #1 Insecticide (pH = 6) #2 Insecticide (DH = 5) Component Wt. % Dursban 0.98 Pyrocide 175 0.06 Piperonyl butoxide 0.13 MGK 264 0.20 Water (distilled) 63.63 Dimethyl ether 35.00 #3 Room Freshener (pH = 6) Component Wt. % Fragrance 1.40 Ethanol (SDA-40-1) 19.60 Water (distilled) 49.00 Dimethyl ether 30.00 #4 Insecticide (DH = 5) Procedure All of the examples were prepared using the following procedure. The active ingredients were weighed individually into an eight-ounce (0.24 ℓ) three-piece aerosol can 5.4 cm (2-1/8") in diameter and 14.1 cm (5-9/16") long, except when the corrosion inhibitors were added to the aerosol can as a solution in the propellant (noted in tables). The can was purged with dichlorodifluoromethane (FC-12) vapor to displace the air in the container. The aerosol can valve was then placed into the can and crimped. The propellants were introduced into the can as liquids through the aerosol valve. Volume amounts corresponding to the weights of the propellants were calculated prior to loading, and a glass, calibrated, pressure buret was used to measure and transfer the liquids from storage cylinders to the can. A nitrogen gas pressure of 6.89·10 5 Pa (100 psig) was applied to the buret to aid in transferring the liquids from the buret to the can. After the propellant was loaded, the can was weighed, and the weight of propellant recorded. The aerosol cans used in the corrosion tests were commercially available container and are described in trade literature as: one inch (2.54 cm) round dome top unlined aerosol containers, size 202 x 509 5.4 cm (2-1/8") diameter, 14.1 cm (5-9/16") can wall height), (0.25 lb). electrolytic tin-plated (ETP), full 113.4 g concave bottom with welded side seam. A corrosion test rating system was used which provides a complete visual description of the appearance of the interior surface of the tin-plated steel aerosol cans after 60 days storage at 48.9 °C (120°F). CAN CORROSION - RATING SYSTEM Rating Description 0 No Corrosion 1 Trace Corrosion 2 Light Corrosion 3 Moderate Corrosion 4 Heavy Corrosion 5 Severe Corrosion MATERIALS USED IN PREPARATION OF CORROSION INHIBITORS Material Designation and Source Oleic Acid Fisher Scientific Company N-tallow-1,3-diaminopropane dioleate Duomeen TDO (Armak Company) 1-(2-Hydroxyethyl)-2-tall oil-2-imidazoline oleate Witcamine PA-78B (Witco Chemical) CORROSION TEST DATA Corrosion Test Procedure - 60 days at 48.9°C (120°F) Corrosion Test Medium - Formulation #2 Corrosion Inhibitor Wt. % Test Rating Description of Test Can Corrosion None --- 5 Severe corrosion in liquid and vapor phases Duomeen TDO 0.50 2 Light vapor phase corrosion Duomeen TDO 0.50 2 Light vapor phase corrosion As can be seen from Table II, in each case the addition of 0.50 wt. % of corrosion inhibitor prevented more than light corrosion of the interior of the test can with Formulation No. 3. CORROSION TEST DATA Corrosion Test Procedure - 60 days at 48.9°C (120°F) Corrosion Test Medium.- Formulation #3 Corrosion Inhibitor Wt. % Test Rating Description of Test Can Corrosion None --- 5 Bottom detinned; corrosion and detinning in vapor phase Witcamine PA-78B 0.50 1 Slight vapor phase corrosion Duomeen TDO 0.50 2 Slight vapor phase corrosion As can be seen from Table III, in each case the addition of 0.50 wt. % of the corrosion inhibitor prevented more than light corrosion of the interior of the test can with Formulation No. 3.

Claims: A process of inhibiting corrosion in a tin-plated steel aerosol can containing an aqueous aerosol formulation and a propellant comprising contacting the aqueous aerosol fonnulation, the propellant and an effective amount of between 0.1 and 1 wt. % based on the total weight of the aqueous aerosol formulation and the propellant of a neutral corrosion inhibitor compound selected from salts of N-tallow-1,3-diaminopropane and oleic acid, salts of 1-(2-hydroxyethyl)2-tall oil-2-imidazoline and oleic acid with the interior of a tin-plated steel aerosol can. A process according to claim 1 wherein the compound is present in an amount between 0.25 to 0.5 wt. % based on the total weight of the aqueous aerosol formulation and the propellant. Use of a salt selected from salts of N-tallow-1, 3-diaminopropane and oleic acid, salts of 1-(2-hydroxyethyl)2-tall oil-2-imidazoline and oleic acid as a corrosion inhibitor in tin-plated steel aerosol cans containing an aqueous aerosol formulation and a propellant in the absence of a volatile amine.

Inventors: BARTLETT PHILIP LEE, BARTLETT, PHILIP LEE
Applicants: DU PONT, E.I. DU PONT DE NEMOURS AND COMPANY
Application year: 1991
Main classification: C23F11
IPC codes: C09K3, C23F11