Synthetic bar compositions providing source of divalent...

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Reexamination Certificate

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C510S153000, C510S155000, C510S156000, C510S508000

Reexamination Certificate

active

06462004

ABSTRACT:

FIELD OF THE INVENTION
The present invention relates to bar compositions comprising synthetic anionic surfactant, fatty acid soap and free fatty acid and to improved processes of making such bars, particularly with higher quantities of essentially water soluble soap (e.g., soap having solubility equal to or greater than 82/18 tallow coconut soap) than previously thought possible. The invention refers particularly to compositions made using a molten mix process, i.e., where ingredients are mixed at temperatures above about 110° F. before the molten composition is chilled, optionally refined and/or milled, plodded to extrudate (generally in form of extruded “logs”) and cut and stamped into final bars. It is in these molten mix processes where higher levels of soluble soaps are associated with materials becoming soft and sticky and causing finishing problems, especially those related to bar stamping.
BACKGROUND OF THE INVENTION
It is well known to make extruded bar compositions using synthetic anionics (e.g., acyl isethionates, alkyl glyceryl ether sulfates etc.) and fatty acid soap.
The soap in such compositions is generally known to serve a number of purposes. First, it serves to help structure the bars so that they do not readily crumble both when the bar is being “finished” (e.g., extruded, stamped) and also as a final user bar. Fatty acid soap also provides some beneficial user properties such as good lather and a certain skin feel which may be desirable to some consumers. In addition, soap is generally cheaper than most anionics and provides some cost savings.
Despite the advantages noted above, however, the level of soap which can be used in the process for making these bars (e.g., molten process in which ingredients are mixed at a temperatures above about 110° F.) and in which soap is not the main surfactant, has generally been considered to have a cap because excessive levels lead to poor bar finishing properties (e.g. principally in that the bars are stickier and result in problems in bar extrusion and stamping when these stickier bars stick to the machinery). Thus, in a bar typically containing 30-75% of a non-soap anionic surfactant, preferably 35-60% anionic, levels of soluble soap above 5% can lead to the above noted finishing problems.
Without wishing to be bound by theory, at least part of this problem is believed to be due to the fact that increasing soap levels generates soap solutions and/or lyotropic liquid crystal phases with unbound water within the synthetic detergent (syndet) bar formulation. The presence of such phases have the potential to hinder the finishing stages of production, which includes extrusion and stamping, by rendering the material soft and sticky.
Unexpectedly, applicants have found that if a source of divalent cation is provided such that the divalent cation is made available to the mix solution (e.g., to be made available, the source component must have solubility equal to or greater than that of calcium carbonate); and sufficient divalent ion is made available to react with the soluble soap dissolved in the unbound water, the degree of softness and stickiness during final bar production can be lessened or alleviated. Moreover, the use of cation does not significantly affect the foam values of the bars and, even at high levels of cation, acceptable foam values are achieved (e.g., 150 ml or greater as measured in defined foam value test).
U.S. Pat. No. 5,981,451 to Farrell et al. relates to a process for making bars containing a mixture of anionic surfactant and soap but there the process is a non-molten process and the stickiness issues of finishing a bar are primarily encountered when using a molten mix process.
U.S. Pat. No. 4,557,853 to Collins relates to bars containing alkaline earth metal carbonates as skin feel agents. Given the low water solubility of these carbonates, it is believed that the level used (2.4%-5.9% earth metal carbonate as defined by the surfactant to earth metal carbonate ratio) is too low to provide a sufficient amount of divalent ion to control the level of soluble soap in solution. That is, the patent fails to recognize the link between providing available divalent cation which can insolubilize the soap at a certain point in the process and thereby reduce stickiness during the finishing stages of bar processing. It should also be noted that the finishing process is considerably less likely to suffer from soft, sticky material issues when soap is the predominant constituent of the formulation.
WO 95/13356 to Procter & Gamble relates to an acyl isethionate bar containing liquid polyols and magnesium soap. The bars of the subject invention do not require liquid polyols of this reference. (However unnecessary the use of liquid polyols in the subject invention, it should be noted that the inventors do not wish to exclude the possibility of using liquid polyols in formulations). Moreover, the patent does not recognize the need for providing available/excess divalent cations (e.g. to aid as scavengers for otherwise soluble soap during molten mixing where, if not removed, they are believed to be the cause of down-stream “finishing” problems). On the contrary, the patent requires the magnesium soap to stay bound and act as a filler/process aid.
U.S. Pat. No. 5,869,441 to Fair et al. discloses bar compositions comprising novel chelating surfactants derived from ethylenediaminetriacetic acid (EDTA). However, this reference differs from bars of the subject invention for a number of reasons.
First, the subject invention is an extrusion process. The Fair patent is not limited to any process but is probably best suited for cast melt or injection molding process. This is because, for example, levels of most amphoterics (claim (1)(c)) above 3% in synthetic formulation would be almost impossible to extrude and maintain acceptable lather. Similarly with claim (1)(e), if levels of PEG, free fatty acid etc. are used at above 40%, it would be extremely difficult to extrude. In short, Fair simply does not teach or recognize that, in an extrusion process, high levels of multivalent help extrusion when soluble soaps are included in the formula.
Further, one major reason Fair et al. avoids multivalent ions (i.e., they must be used at levels below 1% by wt.) is because they significantly depress lather. That is EDTA is by nature a sequestering agent. In the presence of high levels of soluble, multivalent, inorganic salts, EDTA loses surfactancy, via chelation, resulting in poor lather. As noted, Fair et al. fails to recognize the importance of the presence of multivalent ions in the presence of soluble soaps. Bars of the subject invention may have less than 1% multivalent ions and may also have more than 1% multivalent. Indeed, much higher levels are tolerable while maintaining adequate foaming (e.g., >150 ml).
BRIEF DESCRIPTION OF THE INVENTION
More particularly, the subject invention comprises:
(1) 20% to 75%, preferably 35% to 60% by wt. of an anionic surfactant, preferably alkali metal salt of alkyl isethionate;
(2) about 4 to 20%, more preferably greater than 6 to 12% of a fatty acid soap or soap fraction having a solubility equal to or greater than 82/18 tallow/coconut soap i.e., solubility of 1.1 g/l in water at 40° C.);
(3) 4% to 30%, preferably 10 to 25% free fatty acid;
(4) compound or compounds which is a source of divalent cation; which compound is used in an amount sufficient that, when the divalent source compound is solubilized, it provides sufficient available cation to interact with soluble soap fraction (e.g., tallow/coconut soap mixture) such that there is less soluble soap and an enhancement in bar throughput; said enhancement in throughput being defined either by greater extrusion rate and/or greater number of bars stamped per minute.
The solubility of the divalent cation source may affect the amount of the compound used in the process. Thus, it should be understood, for example, that more calcium carbonate may be needed because the solubility of calcium carbonate is low while, for a more soluble salt such as ma

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