EP0640153A1

EP0640153A1 - Method for cleaning aluminum at low temperatures.

Info

Publication number: EP0640153A1
Application number: EP93911127A
Authority: EP
Inventors: Malcolm David Brown; Shane Peter Lambden
Original assignee: Henkel Corp
Current assignee: Henkel Corp
Priority date: 1992-05-14
Filing date: 1993-05-12
Publication date: 1995-03-01
Anticipated expiration: 2013-05-12
Also published as: CA2135391A1; BR9306357A; KR950701691A; DE69309460D1; JPH07508074A; DE69309460T2; ZA933362B; ATE151120T1; EP0640153B1; GR3023464T3; ES2101315T3; MY110663A; WO1993023590A1; SG68573A1

Abstract

An acidic cleaning process for aluminum, especially aluminum cans, that includes a pre-cleaning washing stage followed by an acid cleaning stage is improved by including in the pre-cleaning washing solution both of (i) a component of polyalkoxylated straight or branched chain alcohol surfactant and (ii) a component of polyalkylene glycol-abietic acid surfactant, which are maintained during the process in a ratio of component (i) to component (ii) within the range from 0.4:1 to 3.0:1. The method is particularly useful when the acid cleaning stage also contains both these types of surfactants, but at a lower ratio. A pre-cleaner replenisher composition comprising water, sulfuric acid, and polyalkoxylated straight or branched chain alcohol surfactant is advantageously used in the process.

Description

Description METHOD FOR CLEA NG ALUMINUM AT LOW TEMPERATURES

Technical Field

This invention relates to the cleaning of aluminum surfaces. In particular, it is directed to the cleaning of the surfaces of aluminum cans formed by a cold forming operation.

5 Background Art

After can formation by cold forming, aluminum fines, lubricating oils and other contaminants remain on the surface. It is necessary to clean the surface thoroughly prior to the further treatment which often includes the application of one or more surface coatings.

10 Early cleaning compositions for aluminum surfaces proposed the use of aque¬ ous acidic compositions either alone or with added fluoride at temperatures in the range of 185 to 200 ° F (85 to 93 ° C). In United States patent 4,009,115 and its Re-Issue No. 32,661, Binns proposed the addition of 0.05 to 0.1 grams per liter of hydrofluoric acid as a means of reducing the processing temperature to within the i5 range of 90 to 135 ° F (32 to 57 ° C). The compositions proposed by Binns preferably contain 0.1 to 10 grams per liter of a surfactant which could be anionic, cationic or nonionic.

King et al. in United States patent specification 3,969,135 proposed the use of an aqueous acidic cleaning composition containing a blend of two surfactants. This

2o composition was also suitable for relatively low temperature use and preferably con¬ tained 0.01 to 0.4 weight percent of a fluoride accelerator. The surfactants proposed by King et al. (hereinafter abbreviated as simply "King") were a polyalkoxylated straight chain alcohol and a polyalkylene glycol-abietic acid surfactant. The King compositions are currently used in one or more, preferably at least two, cleaning

.5 stages in the commercial production of aluminum cans, but not usually in the first stage. Normal current practice is to provide most of the acidity in the precleaning stage, immediately before washing the cans with a cleaner composition as taught by King, by directing part of the acid cleaner washing solution into the pre-cleaner wash¬ ing solution, which otherwise consists largely of tap water, with optional additions of acid. When a second stage acid washing solution as taught by King is used in this manner, the ratio between the two kinds of surfactants normally will be the same in the first stage as in the second, if nothing else is added to the first stage solution, inasmuch as no preferential dragout of one type of surfactant has been observed.

5 Washing operations with solutions that include nonionic surfactants are nor¬ mally conducted at or slightly below the cloud point of the washing solution, which is the temperature at which the surfactant comes out of or goes into aqueous solution with changing temperature. It is a characteristic of most nonionic surfactants, includ¬ ing those taught by King as noted above, that they become less soluble in water as

10 the temperature of an aqueous surfactant composition is raised. At temperatures sig¬ nificantly below the cloud point of a particular composition, foaming of the aqueous solution generally occurs quite easily, and it is desirable to avoid foaming in the present washing operations. If the temperature of the composition is too far above the cloud point, separation of the surfactant from the aqueous medium occurs and ιε leads to a loss of detergent ability and a loss of the actual surfactant material. Accordingly, the present washing operations are normally conducted at or below the cloud point where the detergent ability of the composition is still effective and foaming can be minimized. Disclosure of the Invention

20 Problems to Be Solved by the Invention

While the methods described above are effective in cleaning the aluminum sur¬ faces, removal of oil from the used washing solutions is necessary to prevent environ¬ mental pollution upon discharge of the used solutions. It is therefore an object of the present invention to provide a method which will not only be cost effective but will

25 also allow an easier separation from the used washing solution of the oil which that solution has removed from the washed surface. Another object of the present inven¬ tion is to provide a method of cleaning surfaces which will use the improved cleaning method in conjunction with the composition and equipment of the kind currently used in the production of aluminum cans. Still another object of the invention is to provide

3o a process for satisfactory cleaning at a lower temperature than prior art processes, thereby making more economical operation possible. Other objects will be apparent from the description below. Summary of the Invention In one of its major embodiments, the present invention is based on the discov¬ ery that the ratio of the concentration of polyalkoxylated alcohol surfactant to the concentration of polyalkylene glycol-abietic acid surfactant (this ratio being

5 hereinafter briefly denoted "the surfactant ratio") that is optimum for the acid cleaner stage as taught in the King patent already noted above is not usually optimum for the pre-cleaning stage used immediately before the acid cleaner. In addition, independently, it has been discovered that the acid composition normally used in an acid cleaning solution as taught by King can usefully be supplemented with additional ι o sulfuric acid for the pre-cleaner stage. Accordingly, one embodiment of the invention is the provision of a prewashing solution composition with these improved characteristics before, preferably immediately before, a conventional acid cleaning solution in a cleaning operation with at least two stages.

Both these improvements in the pre-cleaner solution can conveniently be is achieved by adding to it during the course of the washing process a replenisher com¬ position that comprises, more preferably consists essentially of, or still more preferably consists of water, sulfuric acid, and a polyalkoxylated straight or branched, but preferably straight, chain alcohol surfactant. The content of sulfuric acid in the replenisher composition is preferably determined by the pH required in use of the

2o composition, and the content of surfactant is adjusted to maintain the stability of the composition. In particular, the composition may contain 5 to 50 per cent by weight of sulfuric acid and 0.5 to 40 per cent by weight of said surfactant.

In the method of one embodiment of the invention, such a composition is add¬ ed to a washing solution as a replenisher composition in a stage preceding, preferably

25 immediately preceding, a conventional acid cleaner stage, such as is taught by Binns or King. The use of such a composition as a replenisher is another aspect of the present invention.

Detailed Description of the invention The pre-cleaner stage of a process according to one embodiment of this inven-

30 tion preferably contains both of (i) a component of polyalkoxylated straight or branched chain, preferably straight chain, alcohol surfactant and (ii) a component of polyalkylene glycol-abietic acid surfactant as taught by King. However, the ratio be- tween these two types in the pre-cleaner stage of a process according to this invention prelsrably is within the range from to 3.0:1, more preferably within the range from 0.7:1 to 2.0:1, still more preferably within the range from 0.9:1.0 to 1.3:1.0, and most preferably within the range from 1.0:1.0 to 1.2:1.0. (In contrast, the most preferred range for the second acid cleaner stage as taught by King, and as preferably used as the next subsequent process in this invention, after the pre-cleaner stage as described above, is about 0.3) Independently, the pH of the pre-cleaning solution in a process according to this invention is preferably within the range from 1.4 to 2.0, more preferably within the range from 1.6 to 2.0, or still more preferably within the range from 1.75 to 1.85, and this pH is preferably achieved by adding to the water used for the pre-cleaning solution only sulfuric acid, in addition to whatever acid is added by countercurrent flow from the subsequent cleaner stage solution.

In a preferred embodiment, the values as described above for the pre-cleaner stage solution are achieved by adding to the original solution during the continued operation of the process a pre-cleaner replenisher composition, in addition to a counterflow from the subsequent acid cleaner solution stage. A pre-cleaner replenisher composition for the present invention comprises, more preferably consists essentially of, or still more preferably consists of, a stable aqueous solution of sulfuric acid with a polyalkoxylated straight or branched chain alcohol surfactant. This improved composition is formulated to be used as a replenisher for the pre- cleaner washing solution which is actually applied to the aluminum surfaces. It may be used alone but is preferably formulated for use in co-operation with the type of composition proposed by King et al., using successive cleaning stages in the can washing equipment. The relative concentration of the components in the composition of the present invention will preferably depend upon the type of system in which the composition is to be used, that is whether the composition is to be used alone or in conjunction with one of the known cleaning compositions.

It has been found that a stable and satisfactory pre-cleaner replenisher compo- sition in accordance with the present invention can be prepared containing 5 to 50 per cent by weight of sulfuric acid and 0.5 to 40 per cent by weight of surfactant. Preferably, the composition contains 30 to 41 per cent by weight of sulfuric acid and 4 to 10 per cent by weight of surfactant; most preferably 41 per cent by weight of sulfuric acid is used. The sulfuric acid content can be varied depending on the way in which the composition is to be used and any such variation will preferably be ac¬ companied by a corresponding variation in the range of surfactant material present. However, once the acid content has been determined, the surfactant content to provide an optimally stable and useful composition can also readily be determined.

The acid content may require variation depending upon the amount and type of material to be cleaned from the surfaces being treated. This will vary with the type of lubricant used in the can formation and with other factors such as the condition of the forming equipment. Suitable polyalkoxylated straight or branched chain alcohol surfactants are known in the art as nonionic surfactants. They include those sold under the trade names Antarox LF 330, Teric 165 and Trycol LF 1. These surfactants are known to have a low cloud point and their use in the present compositions assists in further lowering the temperature at which the washing operation is conducted. It has been found that the compositions of the present invention can be used to significantly lower the pH of the pre-cleaner washing solution in use from the value that it would have if acidified by counterflow from a subsequent acid cleaner stage alone. The reduction in pH which can be thus achieved has been found to improve the cleaning efficiency of the washing solution and the efficiency with which oil can removed.

In a preferred application of the present invention, the improved composition is used in the first of two stages of a washing operation, the second stage using either a known composition of the type proposed by King et al or a composition of this known type modified to co-operate with the composition of the present invention. The following comparison example and example of this preferred use of the invention will further assist an understanding of the benefits which the invention provides. Comparison Example

In a can processing plant including a multi-stage washing section, cans leaving the body maker-trimmer operation section travel on a perforated mat through a pre- cleaner washing stage (stage 1) and then through a cleaner stage (stage 2). In ac¬ cordance with the known washing procedure, washing solution is initially made up with the desired proportion of active ingredients. The composition of the washing so- lution is maintained by the addition of appropriate replenisher compositions to com¬ pensate for the depletion of active materials as the washing procedure continues. The washing solution is sprayed over the can surfaces in the second section and a portion of the washing composition, carrying aluminum, oils, and other materials removed from the can in stage 2, travels in countercurrent to the movement of the cans to stage 1.

In a typical operation using a composition of the type suggested by King et al, the washing solution used in the stage 2 process contains a polyalkylene glycol-abietic acid surfactant blended with a polyalkoxylated straight or branched chain alcohol. A typical washing solution containing approximately 0.065 per cent of the abietic acid derivative sold under the trade designation Teric RA 1315 and approximately 0.023 per cent of the polyalkoxylated straight chain alcohol sold under the trade name Antarox LF 330, as well as sulfuric acid and hydrofluoric acid, provides eight points of free acid in stage 2 at a pH of approximately 1.2. The amount of surfactant blend and acids used in accordance with this process may be varied to provide between 3 to 20 points of free acid.

The washing solution from stage 2 is counterflowed to stage 1 at a rate deter¬ mined by measuring the amount of dissolved aluminum in the solution. The amount of sulfuric acid in the washing solution is depleted because the acid dissolves alumi- num in the course of its cleaning action. The balance of active components in the acid cleaner washing solution is maintained, most preferably by the addition of appropriate amounts of a replenisher composition. (This replenisher composition for the acid cleaner will normally have different composition from the pre-cleaner replenisher that is part of this invention.) In a typical can washer, for a flow rate of washing solution from stage 2 to stage 1 of five liters per minute, the amount of active acid cleaner replenisher compo¬ sition is approximately 65 milliliters per minute. The rate at which the washing solution from stage 2 is added to the stage 1 washing process is also controlled to determine the amount of free acid remaining in the washing solution used in pre- cleaner stage 1. If the acid washing solution is added to stage 1 to provide one point of free acid, the pH is approximately 2.1. If two points of free acid are added by the stage 2 washing solution to stage 1, the pH is approximately 1.8. Example According to the Present Invention

The known process described above can be improved by using a pre-cleaner replenisher composition according to the present invention. Thus a pre-cleaner re¬ plenisher composition as described above can be added to stage 1 to supplement the free acid content of the total washing solution in this stage. For example, if approximately one point of free acid in stage 1 is contributed by the counterfiow of the washing solution from stage 2, and approximately one point of free acid is contributed by a preferred pre-cleaner replenisher composition for the present invention, the additional polyalkoxylated straight or branched chain alcohol added by the composition of the present invention changes the ratio of the concentration of polyalkoxylated alcohol surfactant to the concentration of polyalkylene glycol-abietic acid surfactant ("the surfactant ratio") from approximately 0.3 to approximately 1.1, thus significantly lowering the cloud point of the stage 1 washing solution. This addition also alters the pH from approximately 2.1 to approximately 1.8. It has been found that changing the surfactant ratio, by the addition of polyal¬ koxylated straight or branched chain alcohol surfactant, to the stage 1 washing solution can lead to a reduction of approximately 10 ° C in the cloud point. The extent to which the cloud point is lowered will directly influence the extent to which oil is separated from the washing solution. Based on the use of approximately 65 milliliters of active replenisher composi¬ tion per minute in the counterflowed stage 2 washing solution being required to main¬ tain one point free acid in the stage one process, the amount of pre-cleaner replenisher composition according to the present invention required would be approximately 32 milliliters per minute or 50 liters per day. Use of an improved pre-cleaner replenishing composition of the invention as described in the preceding example can be modified in accordance with the required flow rates necessary to achieve efficient cleaning of the particular cans being processed and more efficient oil removal from the washing solution. In addition, the composition of the (generally different) replenisher solution added to the stage 2 cleaning process can be varied to take into account the effect of the improved cleaning achieved in the stage 1 process by use of the cleaning composition of the present invention. The composition of the replenisher added to the stage 2 processing may also be varied to allow for the effect, on the concentrations and ratios of its active materials, of the materials which may be carried over into the stage 2 process, by the cans moving from stage 1, when an improved composition according to this invention is used for the washing solution in pre-cleaner stage 1.

Claims

1. A can washing process comprising passing initially soiled aluminum cans through a pre-cleaner washing stage and a subsequent acid cleaner stage, characterized in that the washing solution in the pre-cleaner washing stage comprises

5 both of (i) a component of polyalkoxylated straight or branched chain alcohol surfactant and (ii) a component of polyalkylene glycol-abietic acid surfactant, which are maintained during the course of the process in a ratio of component (i) to component (ii) within the range from 0.4:1 to 3.0:1.

2. A process according to claim 1 , wherein the ratio of component (i) to compon- ιo ent (ii) is within the range from 0.7:1 to 2.0:1.

3. A process according to claim 2, wherein the ratio of component (i) to compon¬ ent (ii) is within the range from 0.9:1.0 to 1.3:1.0, and component (i) is selected from polyalkoxylated straight chain alcohols.

4. A process according to claim 3, wherein the pH of the washing solution in the ie pre-cleaner washing stage is maintained during the course of the process within the range from 1.75 to 1.85.

5. A process according to claim 2, wherein the pH of the washing solution in the pre-cleaner washing stage is maintained during the course of the process within the range from 1.6 to 2.0.

20 6. A process according to claim 1 , wherein the pH of the washing solution in the pre-cleaner washing stage is maintained during the course of the process within the range from 1.4 to 2.0.

7. A process according to any one of claims 1 to 6, wherein the washing solution for the acid cleaner stage comprises both of (i) a component of polyalkoxylated straight or branched chain alcohol surfactant and (ii) a component of polyalkylene gly¬ col-abietic acid surfactant, which are maintained during the course of the process in

5 a ratio of component (i) to component (ii) less than 0.4:1; during the course of the process, a portion of the washing solution from the acid cleaner stage is countercur- rently introduced into the pre-cleaner washing solution; and during the course of the process, a pre-cleaner replenisher composition consisting essentially of water, sulfuric acid, and a component of polyalkoxylated straight or branched chain alcohol ιo surfactant is also introduced into the pre-cleaner washing solution.

8. A process according to claim 7, wherein the pre-cleaner replenisher composi¬ tion contains 5 to 50 per cent by weight of sulfuric acid and 0.5 to 40 per cent by weight of surfactant.

9. A process according to claim 8, wherein the pre-cleaner replenisher composi- ιε tion contains 30 to 41 per cent by weight of sulfuric acid and 4 to 10 per cent by weight of surfactant.

10. The use of a stable aqueous solution consisting essentially of water, sulfuric acid, and a component of polyalkoxylated straight or branched chain alcohol surfactant as a pre-cleaner replenisher composition to lower the pH of the washing

20 solution in the pre-cleaning stage of a washing process containing at least two stages, including an acid cleaning stage following said pre-cleaning stage, for cleaning initially soiled aluminum cans.

11. A use according to claim 10, wherein the pre-cleaner replenisher composition contains 5 to 50 per cent by weight of sulfuric acid, and 0.5 to 40 per cent by weight

25 of surfactant.

12. A use according to claim 11, wherein the pre-cleaner replenisher composition contains 30 to 41 per cent by weight of sulfuric acid and 4 to 10 per cent by weight of surfactant.